Mixture of 2-Butanone + Ethanol

Datasets

1. Mole fraction (12)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (4)
6. c_sound,fluid - Speed of Sound, m/s (2)
7. T_boil - Boiling temperature at pressure P, K (8)
8. Azeotropic temperature, K (2)

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	0.0000
0.0360	0.0600
0.0700	0.1120
0.1060	0.1610
0.1420	0.2050
0.1970	0.2700
0.2580	0.3320
0.3050	0.3680
0.3740	0.4200
0.4320	0.4540
0.4910	0.4950
0.5430	0.5340
0.5970	0.5650
0.6440	0.6040
0.6950	0.6420
0.7520	0.6920
0.7870	0.7290
0.8420	0.7810
0.8980	0.8410
0.9580	0.9140
1.0000	1.0000

Azeotropic composition: mole fraction of Ethanol (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethanol (2) - Liquid
101.30	0.5040

Mole fraction of 2-Butanone (1) [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Gas	Pressure, kPa - Liquid	Mole fraction of 2-Butanone (1) - Liquid
0.0000	20.00	0.0000
0.0000	101.30	0.0000
0.0740	101.30	0.0430
0.1180	20.00	0.0460
0.1410	101.30	0.0880
0.1910	20.00	0.0780
0.1980	101.30	0.1340
0.2450	101.30	0.1790
0.2560	20.00	0.1210
0.3000	101.30	0.2360
0.3130	20.00	0.1680
0.3440	101.30	0.2910
0.3660	20.00	0.2080
0.3830	101.30	0.3430
0.4180	101.30	0.3920
0.4200	20.00	0.2670
0.4550	101.30	0.4410
0.4620	20.00	0.3200
0.4940	101.30	0.4990
0.5010	20.00	0.3700
0.5330	20.00	0.4210
0.5330	101.30	0.5540
0.5640	20.00	0.4720
0.5700	101.30	0.6080
0.5950	20.00	0.5230
0.6040	101.30	0.6550
0.6240	20.00	0.5730
0.6400	101.30	0.7040
0.6580	20.00	0.6280
0.6880	101.30	0.7550
0.6890	20.00	0.6780
0.7260	20.00	0.7370
0.7340	101.30	0.8010
0.7660	20.00	0.7930
0.7850	101.30	0.8600
0.8130	20.00	0.8530
0.8520	101.30	0.9130
0.8680	20.00	0.9080
0.9170	101.30	0.9600
0.9380	20.00	0.9640
1.0000	20.00	1.0000
1.0000	101.30	1.0000

Mole fraction of 2-Butanone (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Mole fraction of 2-Butanone (1) - Gas
0.0000	0.0000
0.0290	0.0500
0.0630	0.1010
0.0940	0.1430
0.1390	0.1960
0.1800	0.2410
0.2370	0.2970
0.3320	0.3740
0.4290	0.4450
0.4700	0.4760
0.5440	0.5270
0.6380	0.5890
0.7440	0.6760
0.8150	0.7470
0.8520	0.7850
0.9060	0.8490
0.9450	0.9030
0.9740	0.9510
1.0000	1.0000

Mole fraction of 2-Butanone (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Mole fraction of 2-Butanone (1) - Gas
0.0000	0.0000
0.0290	0.0500
0.0630	0.1010
0.0940	0.1430
0.1390	0.1960
0.1800	0.2410
0.2370	0.2970
0.3320	0.3740
0.4290	0.4450
0.4700	0.4760
0.5440	0.5270
0.6380	0.5890
0.7440	0.6760
0.8150	0.7470
0.8520	0.7850
0.9060	0.8490
0.9450	0.9030
0.9740	0.9510
1.0000	1.0000

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	383.30	0.0000
0.1110	383.30	0.1870
0.1600	383.30	0.2440
0.2310	383.30	0.3280
0.2900	383.30	0.3930
0.3580	383.30	0.4500
0.4650	383.30	0.5270
0.6450	383.30	0.6700
0.7550	383.30	0.7520
0.8580	383.30	0.8420
1.0000	383.30	1.0000
0.0000	398.20	0.0000
0.1350	398.20	0.2210
0.2020	398.20	0.3040
0.2440	398.20	0.3580
0.3580	398.20	0.4700
0.5370	398.20	0.6070
0.5880	398.20	0.6510
0.7490	398.20	0.7680
0.8420	398.20	0.8430
1.0000	398.20	1.0000
0.0000	413.20	0.0000
0.1220	413.20	0.2070
0.2080	413.20	0.3200
0.2950	413.20	0.4190
0.3700	413.20	0.4910
0.4920	413.20	0.5920
0.5540	413.20	0.6400
0.6410	413.20	0.7030
0.7180	413.20	0.7590
0.8350	413.20	0.8430
0.9000	413.20	0.9030
0.9160	413.20	0.9190
1.0000	413.20	1.0000

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	0.0000
0.0360	0.0600
0.0700	0.1120
0.1060	0.1610
0.1420	0.2050
0.1970	0.2700
0.2580	0.3320
0.3050	0.3680
0.3740	0.4200
0.4320	0.4540
0.4910	0.4950
0.5430	0.5340
0.5970	0.5650
0.6440	0.6040
0.6950	0.6420
0.7520	0.6920
0.7870	0.7290
0.8420	0.7810
0.8980	0.8410
0.9580	0.9140
1.0000	1.0000

Azeotropic composition: mole fraction of Ethanol (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Ethanol (2) - Liquid
101.30	0.5040

Mole fraction of 2-Butanone (1) [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Gas	Pressure, kPa - Liquid	Mole fraction of 2-Butanone (1) - Liquid
0.0000	20.00	0.0000
0.0000	101.30	0.0000
0.0740	101.30	0.0430
0.1180	20.00	0.0460
0.1410	101.30	0.0880
0.1910	20.00	0.0780
0.1980	101.30	0.1340
0.2450	101.30	0.1790
0.2560	20.00	0.1210
0.3000	101.30	0.2360
0.3130	20.00	0.1680
0.3440	101.30	0.2910
0.3660	20.00	0.2080
0.3830	101.30	0.3430
0.4180	101.30	0.3920
0.4200	20.00	0.2670
0.4550	101.30	0.4410
0.4620	20.00	0.3200
0.4940	101.30	0.4990
0.5010	20.00	0.3700
0.5330	20.00	0.4210
0.5330	101.30	0.5540
0.5640	20.00	0.4720
0.5700	101.30	0.6080
0.5950	20.00	0.5230
0.6040	101.30	0.6550
0.6240	20.00	0.5730
0.6400	101.30	0.7040
0.6580	20.00	0.6280
0.6880	101.30	0.7550
0.6890	20.00	0.6780
0.7260	20.00	0.7370
0.7340	101.30	0.8010
0.7660	20.00	0.7930
0.7850	101.30	0.8600
0.8130	20.00	0.8530
0.8520	101.30	0.9130
0.8680	20.00	0.9080
0.9170	101.30	0.9600
0.9380	20.00	0.9640
1.0000	20.00	1.0000
1.0000	101.30	1.0000

Mole fraction of 2-Butanone (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Mole fraction of 2-Butanone (1) - Gas
0.0000	0.0000
0.0290	0.0500
0.0630	0.1010
0.0940	0.1430
0.1390	0.1960
0.1800	0.2410
0.2370	0.2970
0.3320	0.3740
0.4290	0.4450
0.4700	0.4760
0.5440	0.5270
0.6380	0.5890
0.7440	0.6760
0.8150	0.7470
0.8520	0.7850
0.9060	0.8490
0.9450	0.9030
0.9740	0.9510
1.0000	1.0000

Mole fraction of 2-Butanone (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Mole fraction of 2-Butanone (1) - Gas
0.0000	0.0000
0.0290	0.0500
0.0630	0.1010
0.0940	0.1430
0.1390	0.1960
0.1800	0.2410
0.2370	0.2970
0.3320	0.3740
0.4290	0.4450
0.4700	0.4760
0.5440	0.5270
0.6380	0.5890
0.7440	0.6760
0.8150	0.7470
0.8520	0.7850
0.9060	0.8490
0.9450	0.9030
0.9740	0.9510
1.0000	1.0000

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	383.30	0.0000
0.1110	383.30	0.1870
0.1600	383.30	0.2440
0.2310	383.30	0.3280
0.2900	383.30	0.3930
0.3580	383.30	0.4500
0.4650	383.30	0.5270
0.6450	383.30	0.6700
0.7550	383.30	0.7520
0.8580	383.30	0.8420
1.0000	383.30	1.0000
0.0000	398.20	0.0000
0.1350	398.20	0.2210
0.2020	398.20	0.3040
0.2440	398.20	0.3580
0.3580	398.20	0.4700
0.5370	398.20	0.6070
0.5880	398.20	0.6510
0.7490	398.20	0.7680
0.8420	398.20	0.8430
1.0000	398.20	1.0000
0.0000	413.20	0.0000
0.1220	413.20	0.2070
0.2080	413.20	0.3200
0.2950	413.20	0.4190
0.3700	413.20	0.4910
0.4920	413.20	0.5920
0.5540	413.20	0.6400
0.6410	413.20	0.7030
0.7180	413.20	0.7590
0.8350	413.20	0.8430
0.9000	413.20	0.9030
0.9160	413.20	0.9190
1.0000	413.20	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0004
298.15	0.0500	0.0004
298.15	0.1000	0.0004
298.15	0.1500	0.0004
298.15	0.2000	0.0004
298.15	0.2500	0.0004
298.15	0.3000	0.0004
298.15	0.3500	0.0004
298.15	0.4000	0.0004
298.15	0.4500	0.0005
298.15	0.5000	0.0005
298.15	0.5500	0.0005
298.15	0.6000	0.0005
298.15	0.6500	0.0006
298.15	0.7000	0.0006
298.15	0.7500	0.0007
298.15	0.8000	0.0007
298.15	0.8500	0.0008
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0003
308.15	0.0500	0.0003
308.15	0.1000	0.0003
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0004
308.15	0.3500	0.0004
308.15	0.4000	0.0004
308.15	0.4500	0.0004
308.15	0.5000	0.0004
308.15	0.5500	0.0004
308.15	0.6000	0.0005
308.15	0.6500	0.0005
308.15	0.7000	0.0005
308.15	0.7500	0.0006
308.15	0.8000	0.0006
308.15	0.8500	0.0007
308.15	0.9000	0.0007
308.15	0.9500	0.0008
308.15	1.0000	0.0009
318.15	0.0000	0.0003
318.15	0.0500	0.0003
318.15	0.1000	0.0003
318.15	0.1500	0.0003
318.15	0.2000	0.0003
318.15	0.2500	0.0003
318.15	0.3000	0.0003
318.15	0.3500	0.0003
318.15	0.4000	0.0004
318.15	0.4500	0.0004
318.15	0.5000	0.0004
318.15	0.5500	0.0004
318.15	0.6000	0.0004
318.15	0.6500	0.0004
318.15	0.7000	0.0005
318.15	0.7500	0.0005
318.15	0.8000	0.0005
318.15	0.8500	0.0006
318.15	0.9000	0.0006
318.15	0.9500	0.0007
318.15	1.0000	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0004
298.15	0.0500	0.0004
298.15	0.1000	0.0004
298.15	0.1500	0.0004
298.15	0.2000	0.0004
298.15	0.2500	0.0004
298.15	0.3000	0.0004
298.15	0.3500	0.0004
298.15	0.4000	0.0004
298.15	0.4500	0.0005
298.15	0.5000	0.0005
298.15	0.5500	0.0005
298.15	0.6000	0.0005
298.15	0.6500	0.0006
298.15	0.7000	0.0006
298.15	0.7500	0.0007
298.15	0.8000	0.0007
298.15	0.8500	0.0008
298.15	0.9000	0.0009
298.15	0.9500	0.0010
298.15	1.0000	0.0011
308.15	0.0000	0.0003
308.15	0.0500	0.0003
308.15	0.1000	0.0003
308.15	0.1500	0.0004
308.15	0.2000	0.0004
308.15	0.2500	0.0004
308.15	0.3000	0.0004
308.15	0.3500	0.0004
308.15	0.4000	0.0004
308.15	0.4500	0.0004
308.15	0.5000	0.0004
308.15	0.5500	0.0004
308.15	0.6000	0.0005
308.15	0.6500	0.0005
308.15	0.7000	0.0005
308.15	0.7500	0.0006
308.15	0.8000	0.0006
308.15	0.8500	0.0007
308.15	0.9000	0.0007
308.15	0.9500	0.0008
308.15	1.0000	0.0009
318.15	0.0000	0.0003
318.15	0.0500	0.0003
318.15	0.1000	0.0003
318.15	0.1500	0.0003
318.15	0.2000	0.0003
318.15	0.2500	0.0003
318.15	0.3000	0.0003
318.15	0.3500	0.0003
318.15	0.4000	0.0004
318.15	0.4500	0.0004
318.15	0.5000	0.0004
318.15	0.5500	0.0004
318.15	0.6000	0.0004
318.15	0.6500	0.0004
318.15	0.7000	0.0005
318.15	0.7500	0.0005
318.15	0.8000	0.0005
318.15	0.8500	0.0006
318.15	0.9000	0.0006
318.15	0.9500	0.0007
318.15	1.0000	0.0008

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	383.30	245.60
0.1110	383.30	271.60
0.1600	383.30	279.80
0.2310	383.30	290.30
0.2900	383.30	297.90
0.3580	383.30	304.50
0.4650	383.30	314.00
0.6450	383.30	321.80
0.7550	383.30	323.10
0.8580	383.30	322.00
1.0000	383.30	315.60
0.0000	398.20	358.50
0.1350	398.20	405.60
0.2020	398.20	423.50
0.2440	398.20	433.90
0.3580	398.20	457.40
0.5370	398.20	483.30
0.5880	398.20	488.40
0.7490	398.20	499.30
0.8420	398.20	501.40
1.0000	398.20	498.30
0.0000	413.20	506.60
0.1220	413.20	572.60
0.2080	413.20	607.70
0.2950	413.20	639.50
0.3700	413.20	662.70
0.4920	413.20	695.70
0.5540	413.20	710.20
0.6410	413.20	726.70
0.7180	413.20	740.70
0.8350	413.20	753.80
0.9000	413.20	756.90
0.9160	413.20	758.70
1.0000	413.20	757.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	383.30	245.60
0.1110	383.30	271.60
0.1600	383.30	279.80
0.2310	383.30	290.30
0.2900	383.30	297.90
0.3580	383.30	304.50
0.4650	383.30	314.00
0.6450	383.30	321.80
0.7550	383.30	323.10
0.8580	383.30	322.00
1.0000	383.30	315.60
0.0000	398.20	358.50
0.1350	398.20	405.60
0.2020	398.20	423.50
0.2440	398.20	433.90
0.3580	398.20	457.40
0.5370	398.20	483.30
0.5880	398.20	488.40
0.7490	398.20	499.30
0.8420	398.20	501.40
1.0000	398.20	498.30
0.0000	413.20	506.60
0.1220	413.20	572.60
0.2080	413.20	607.70
0.2950	413.20	639.50
0.3700	413.20	662.70
0.4920	413.20	695.70
0.5540	413.20	710.20
0.6410	413.20	726.70
0.7180	413.20	740.70
0.8350	413.20	753.80
0.9000	413.20	756.90
0.9160	413.20	758.70
1.0000	413.20	757.00

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3788
293.15	0.0497	1.3784
293.15	0.0983	1.3779
293.15	0.1983	1.3769
293.15	0.2956	1.3757
293.15	0.4006	1.3743
293.15	0.5012	1.3728
293.15	0.6063	1.3709
293.15	0.7002	1.369
293.15	0.7995	1.3667
293.15	0.8994	1.3643
293.15	0.9518	1.3629
293.15	1.0000	1.3614
298.15	0.0000	1.3762
298.15	0.0497	1.3758
298.15	0.0983	1.3753
298.15	0.1983	1.3743
298.15	0.2956	1.3732
298.15	0.4006	1.3719
298.15	0.5012	1.3704
298.15	0.6063	1.3685
298.15	0.7002	1.3667
298.15	0.7995	1.3645
298.15	0.8994	1.3621
298.15	0.9518	1.3607
298.15	1.0000	1.3593
303.15	0.0000	1.3736
303.15	0.0497	1.3732
303.15	0.0983	1.3727
303.15	0.1983	1.3717
303.15	0.2956	1.3706
303.15	0.4006	1.3694
303.15	0.5012	1.368
303.15	0.6063	1.3662
303.15	0.7002	1.3644
303.15	0.7995	1.3622
303.15	0.8994	1.3599
303.15	0.9518	1.3586
303.15	1.0000	1.3573

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3788
293.15	0.0497	1.3784
293.15	0.0983	1.3779
293.15	0.1983	1.3769
293.15	0.2956	1.3757
293.15	0.4006	1.3743
293.15	0.5012	1.3728
293.15	0.6063	1.3709
293.15	0.7002	1.369
293.15	0.7995	1.3667
293.15	0.8994	1.3643
293.15	0.9518	1.3629
293.15	1.0000	1.3614
298.15	0.0000	1.3762
298.15	0.0497	1.3758
298.15	0.0983	1.3753
298.15	0.1983	1.3743
298.15	0.2956	1.3732
298.15	0.4006	1.3719
298.15	0.5012	1.3704
298.15	0.6063	1.3685
298.15	0.7002	1.3667
298.15	0.7995	1.3645
298.15	0.8994	1.3621
298.15	0.9518	1.3607
298.15	1.0000	1.3593
303.15	0.0000	1.3736
303.15	0.0497	1.3732
303.15	0.0983	1.3727
303.15	0.1983	1.3717
303.15	0.2956	1.3706
303.15	0.4006	1.3694
303.15	0.5012	1.368
303.15	0.6063	1.3662
303.15	0.7002	1.3644
303.15	0.7995	1.3622
303.15	0.8994	1.3599
303.15	0.9518	1.3586
303.15	1.0000	1.3573

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	805.6
293.15	0.0497	805.2
293.15	0.0983	804.8
293.15	0.1983	803.8
293.15	0.2956	802.7
293.15	0.4006	801.4
293.15	0.5012	800.0
293.15	0.6063	798.4
293.15	0.7002	796.8
293.15	0.7995	794.8
293.15	0.8994	792.4
293.15	0.9518	790.9
293.15	1.0000	789.3
298.15	0.0000	799.7
298.15	0.0497	799.4
298.15	0.0983	799.0
298.15	0.1983	798.0
298.15	0.2956	797.1
298.15	0.4006	795.9
298.15	0.5012	794.7
298.15	0.6063	793.3
298.15	0.7002	791.9
298.15	0.7995	790.0
298.15	0.8994	787.9
298.15	0.9518	786.5
298.15	1.0000	785.1
303.15	0.0000	794.9
303.15	0.0497	794.5
303.15	0.0983	794.2
303.15	0.1983	793.3
303.15	0.2956	792.3
303.15	0.4006	791.2
303.15	0.5012	790.1
303.15	0.6063	788.7
303.15	0.7002	787.3
303.15	0.7995	785.5
303.15	0.8994	783.4
303.15	0.9518	782.1
303.15	1.0000	780.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	799.7
298.15	0.0500	799.3
298.15	0.1000	798.9
298.15	0.1500	798.4
298.15	0.2000	797.9
298.15	0.2500	797.4
298.15	0.3000	796.9
298.15	0.3500	796.4
298.15	0.4000	795.8
298.15	0.4500	795.2
298.15	0.5000	794.6
298.15	0.5500	794.0
298.15	0.6000	793.3
298.15	0.6500	792.6
298.15	0.7000	791.8
298.15	0.7500	790.9
298.15	0.8000	790.0
298.15	0.8500	788.9
298.15	0.9000	787.8
298.15	0.9500	786.6
298.15	1.0000	785.1
308.15	0.0000	789.2
308.15	0.0500	788.8
308.15	0.1000	788.3
308.15	0.1500	787.9
308.15	0.2000	787.4
308.15	0.2500	787.0
308.15	0.3000	786.5
308.15	0.3500	786.1
308.15	0.4000	785.6
308.15	0.4500	785.1
308.15	0.5000	784.6
308.15	0.5500	784.0
308.15	0.6000	783.4
308.15	0.6500	782.8
308.15	0.7000	782.1
308.15	0.7500	781.4
308.15	0.8000	780.6
308.15	0.8500	779.7
308.15	0.9000	778.7
308.15	0.9500	777.7
308.15	1.0000	776.5
318.15	0.0000	778.4
318.15	0.0500	778.0
318.15	0.1000	777.6
318.15	0.1500	777.2
318.15	0.2000	776.8
318.15	0.2500	776.4
318.15	0.3000	776.0
318.15	0.3500	775.6
318.15	0.4000	775.2
318.15	0.4500	774.7
318.15	0.5000	774.3
318.15	0.5500	773.8
318.15	0.6000	773.3
318.15	0.6500	772.8
318.15	0.7000	772.2
318.15	0.7500	771.6
318.15	0.8000	771.0
318.15	0.8500	770.3
318.15	0.9000	769.5
318.15	0.9500	768.6
318.15	1.0000	767.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	805.6
293.15	0.0497	805.2
293.15	0.0983	804.8
293.15	0.1983	803.8
293.15	0.2956	802.7
293.15	0.4006	801.4
293.15	0.5012	800.0
293.15	0.6063	798.4
293.15	0.7002	796.8
293.15	0.7995	794.8
293.15	0.8994	792.4
293.15	0.9518	790.9
293.15	1.0000	789.3
298.15	0.0000	799.7
298.15	0.0497	799.4
298.15	0.0983	799.0
298.15	0.1983	798.0
298.15	0.2956	797.1
298.15	0.4006	795.9
298.15	0.5012	794.7
298.15	0.6063	793.3
298.15	0.7002	791.9
298.15	0.7995	790.0
298.15	0.8994	787.9
298.15	0.9518	786.5
298.15	1.0000	785.1
303.15	0.0000	794.9
303.15	0.0497	794.5
303.15	0.0983	794.2
303.15	0.1983	793.3
303.15	0.2956	792.3
303.15	0.4006	791.2
303.15	0.5012	790.1
303.15	0.6063	788.7
303.15	0.7002	787.3
303.15	0.7995	785.5
303.15	0.8994	783.4
303.15	0.9518	782.1
303.15	1.0000	780.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	799.7
298.15	0.0500	799.3
298.15	0.1000	798.9
298.15	0.1500	798.4
298.15	0.2000	797.9
298.15	0.2500	797.4
298.15	0.3000	796.9
298.15	0.3500	796.4
298.15	0.4000	795.8
298.15	0.4500	795.2
298.15	0.5000	794.6
298.15	0.5500	794.0
298.15	0.6000	793.3
298.15	0.6500	792.6
298.15	0.7000	791.8
298.15	0.7500	790.9
298.15	0.8000	790.0
298.15	0.8500	788.9
298.15	0.9000	787.8
298.15	0.9500	786.6
298.15	1.0000	785.1
308.15	0.0000	789.2
308.15	0.0500	788.8
308.15	0.1000	788.3
308.15	0.1500	787.9
308.15	0.2000	787.4
308.15	0.2500	787.0
308.15	0.3000	786.5
308.15	0.3500	786.1
308.15	0.4000	785.6
308.15	0.4500	785.1
308.15	0.5000	784.6
308.15	0.5500	784.0
308.15	0.6000	783.4
308.15	0.6500	782.8
308.15	0.7000	782.1
308.15	0.7500	781.4
308.15	0.8000	780.6
308.15	0.8500	779.7
308.15	0.9000	778.7
308.15	0.9500	777.7
308.15	1.0000	776.5
318.15	0.0000	778.4
318.15	0.0500	778.0
318.15	0.1000	777.6
318.15	0.1500	777.2
318.15	0.2000	776.8
318.15	0.2500	776.4
318.15	0.3000	776.0
318.15	0.3500	775.6
318.15	0.4000	775.2
318.15	0.4500	774.7
318.15	0.5000	774.3
318.15	0.5500	773.8
318.15	0.6000	773.3
318.15	0.6500	772.8
318.15	0.7000	772.2
318.15	0.7500	771.6
318.15	0.8000	771.0
318.15	0.8500	770.3
318.15	0.9000	769.5
318.15	0.9500	768.6
318.15	1.0000	767.7

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1212.0
293.15	0.0497	1214.0
293.15	0.0983	1213.0
293.15	0.1983	1210.0
293.15	0.2956	1206.0
293.15	0.4006	1202.0
293.15	0.5012	1197.0
293.15	0.6063	1193.0
293.15	0.7002	1187.0
293.15	0.7995	1180.0
293.15	0.8994	1172.0
293.15	0.9518	1166.0
293.15	1.0000	1160.0
298.15	0.0000	1192.0
298.15	0.0497	1192.0
298.15	0.0983	1192.0
298.15	0.1983	1189.0
298.15	0.2956	1186.0
298.15	0.4006	1182.0
298.15	0.5012	1177.0
298.15	0.6063	1173.0
298.15	0.7002	1168.0
298.15	0.7995	1162.0
298.15	0.8994	1154.0
298.15	0.9518	1149.0
298.15	1.0000	1143.0
303.15	0.0000	1163.0
303.15	0.0497	1162.0
303.15	0.0983	1162.0
303.15	0.1983	1161.0
303.15	0.2956	1159.0
303.15	0.4006	1156.0
303.15	0.5012	1153.0
303.15	0.6063	1150.0
303.15	0.7002	1147.0
303.15	0.7995	1142.0
303.15	0.8994	1136.0
303.15	0.9518	1131.0
303.15	1.0000	1127.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1212.0
293.15	0.0497	1214.0
293.15	0.0983	1213.0
293.15	0.1983	1210.0
293.15	0.2956	1206.0
293.15	0.4006	1202.0
293.15	0.5012	1197.0
293.15	0.6063	1193.0
293.15	0.7002	1187.0
293.15	0.7995	1180.0
293.15	0.8994	1172.0
293.15	0.9518	1166.0
293.15	1.0000	1160.0
298.15	0.0000	1192.0
298.15	0.0497	1192.0
298.15	0.0983	1192.0
298.15	0.1983	1189.0
298.15	0.2956	1186.0
298.15	0.4006	1182.0
298.15	0.5012	1177.0
298.15	0.6063	1173.0
298.15	0.7002	1168.0
298.15	0.7995	1162.0
298.15	0.8994	1154.0
298.15	0.9518	1149.0
298.15	1.0000	1143.0
303.15	0.0000	1163.0
303.15	0.0497	1162.0
303.15	0.0983	1162.0
303.15	0.1983	1161.0
303.15	0.2956	1159.0
303.15	0.4006	1156.0
303.15	0.5012	1153.0
303.15	0.6063	1150.0
303.15	0.7002	1147.0
303.15	0.7995	1142.0
303.15	0.8994	1136.0
303.15	0.9518	1131.0
303.15	1.0000	1127.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	352.72
0.0360	351.69
0.0700	351.00
0.1060	350.36
0.1420	349.71
0.1970	348.90
0.2580	348.32
0.3050	347.95
0.3740	347.69
0.4320	347.55
0.4910	347.48
0.5430	347.50
0.5970	347.56
0.6440	347.70
0.6950	347.91
0.7520	348.21
0.7870	348.58
0.8420	349.06
0.8980	349.70
0.9580	350.45
1.0000	351.44

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Gas	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	20.00	315.41
0.0000	101.30	351.46
0.0740	101.30	350.53
0.1180	20.00	313.91
0.1410	101.30	349.78
0.1910	20.00	312.87
0.1980	101.30	349.19
0.2450	101.30	348.73
0.2560	20.00	311.87
0.3000	101.30	348.29
0.3130	20.00	311.00
0.3440	101.30	347.94
0.3660	20.00	310.30
0.3830	101.30	347.72
0.4180	101.30	347.58
0.4200	20.00	309.69
0.4550	101.30	347.51
0.4620	20.00	309.23
0.4940	101.30	347.50
0.5010	20.00	308.82
0.5330	20.00	308.50
0.5330	101.30	347.54
0.5640	20.00	308.29
0.5700	101.30	347.66
0.5950	20.00	308.12
0.6040	101.30	347.87
0.6240	20.00	307.82
0.6400	101.30	348.10
0.6580	20.00	307.70
0.6880	101.30	348.56
0.6890	20.00	307.64
0.7260	20.00	307.73
0.7340	101.30	348.99
0.7660	20.00	307.87
0.7850	101.30	349.68
0.8130	20.00	308.00
0.8520	101.30	350.44
0.8680	20.00	308.41
0.9170	101.30	351.34
0.9380	20.00	308.94
1.0000	20.00	309.55
1.0000	101.30	352.68

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.45
0.0290	350.78
0.0630	350.21
0.0940	349.79
0.1390	349.25
0.1800	348.85
0.2370	348.31
0.3320	347.79
0.4290	347.54
0.4700	347.50
0.5440	347.51
0.6380	347.72
0.7440	348.35
0.8150	349.08
0.8520	349.63
0.9060	350.59
0.9450	351.34
0.9740	351.89
1.0000	352.72

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.45
0.0290	350.78
0.0630	350.21
0.0940	349.79
0.1390	349.25
0.1800	348.85
0.2370	348.31
0.3320	347.79
0.4290	347.54
0.4700	347.50
0.5440	347.51
0.6380	347.72
0.7440	348.35
0.8150	349.08
0.8520	349.63
0.9060	350.59
0.9450	351.34
0.9740	351.89
1.0000	352.72

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	352.72
0.0360	351.69
0.0700	351.00
0.1060	350.36
0.1420	349.71
0.1970	348.90
0.2580	348.32
0.3050	347.95
0.3740	347.69
0.4320	347.55
0.4910	347.48
0.5430	347.50
0.5970	347.56
0.6440	347.70
0.6950	347.91
0.7520	348.21
0.7870	348.58
0.8420	349.06
0.8980	349.70
0.9580	350.45
1.0000	351.44

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Gas	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	20.00	315.41
0.0000	101.30	351.46
0.0740	101.30	350.53
0.1180	20.00	313.91
0.1410	101.30	349.78
0.1910	20.00	312.87
0.1980	101.30	349.19
0.2450	101.30	348.73
0.2560	20.00	311.87
0.3000	101.30	348.29
0.3130	20.00	311.00
0.3440	101.30	347.94
0.3660	20.00	310.30
0.3830	101.30	347.72
0.4180	101.30	347.58
0.4200	20.00	309.69
0.4550	101.30	347.51
0.4620	20.00	309.23
0.4940	101.30	347.50
0.5010	20.00	308.82
0.5330	20.00	308.50
0.5330	101.30	347.54
0.5640	20.00	308.29
0.5700	101.30	347.66
0.5950	20.00	308.12
0.6040	101.30	347.87
0.6240	20.00	307.82
0.6400	101.30	348.10
0.6580	20.00	307.70
0.6880	101.30	348.56
0.6890	20.00	307.64
0.7260	20.00	307.73
0.7340	101.30	348.99
0.7660	20.00	307.87
0.7850	101.30	349.68
0.8130	20.00	308.00
0.8520	101.30	350.44
0.8680	20.00	308.41
0.9170	101.30	351.34
0.9380	20.00	308.94
1.0000	20.00	309.55
1.0000	101.30	352.68

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.45
0.0290	350.78
0.0630	350.21
0.0940	349.79
0.1390	349.25
0.1800	348.85
0.2370	348.31
0.3320	347.79
0.4290	347.54
0.4700	347.50
0.5440	347.51
0.6380	347.72
0.7440	348.35
0.8150	349.08
0.8520	349.63
0.9060	350.59
0.9450	351.34
0.9740	351.89
1.0000	352.72

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 2-Butanone (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	351.45
0.0290	350.78
0.0630	350.21
0.0940	349.79
0.1390	349.25
0.1800	348.85
0.2370	348.31
0.3320	347.79
0.4290	347.54
0.4700	347.50
0.5440	347.51
0.6380	347.72
0.7440	348.35
0.8150	349.08
0.8520	349.63
0.9060	350.59
0.9450	351.34
0.9740	351.89
1.0000	352.72

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	347.46

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	347.46

Sources

• Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
• Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
• Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 kPa
• Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
• Isothermal Vapor Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell