Mixture of 2-Butanone + Pentane, 2,2,4-trimethyl-

Datasets

1. Mole fraction (8)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (2)
4. T_boil - Boiling temperature at pressure P, K (2)
5. Azeotropic temperature, K (6)

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
0.0300	0.1250
0.0690	0.2290
0.1110	0.3090
0.1520	0.3720
0.2040	0.4450
0.2600	0.4930
0.3130	0.5310
0.3810	0.5670
0.4220	0.5940
0.4770	0.6180
0.5360	0.6490
0.5850	0.6730
0.6360	0.6990
0.6770	0.7260
0.7180	0.7530
0.7890	0.7850
0.8450	0.8250
0.8920	0.8700
0.9430	0.9250
1.0000	1.0000

Azeotropic composition: mole fraction of 2-Butanone (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of 2-Butanone (1) - Liquid
101.30	0.7830

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

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Gas	Mole fraction of 2-Butanone (1) - Gas
20.00	306.97	0.7390
20.00	307.03	0.7100
20.00	307.16	0.6840
20.00	307.42	0.6560
20.00	307.55	0.8280
20.00	307.70	0.6370
20.00	308.16	0.6030
20.00	308.21	0.8950
20.00	308.93	0.5760
20.00	309.23	0.9790
20.00	309.65	1.0000
20.00	309.75	0.5350
20.00	312.33	0.4360
20.00	315.65	0.3110
20.00	323.65	0.0000
20.00	307.16	0.7800
101.30	350.44	0.7580
101.30	350.50	0.7970
101.30	350.60	0.7220
101.30	350.83	0.8440
101.30	351.00	0.6890
101.30	351.46	0.9060
101.30	351.57	0.6590
101.30	352.34	0.6240
101.30	352.38	0.9780
101.30	352.68	1.0000
101.30	353.42	0.5870
101.30	354.95	0.5310
101.30	357.33	0.4590
101.30	361.11	0.3580
101.30	365.99	0.2230
101.30	372.33	0.0000

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

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid
20.00	306.97	0.7430
20.00	307.03	0.6730
20.00	307.16	0.6020
20.00	307.42	0.5320
20.00	307.55	0.8810
20.00	307.70	0.4630
20.00	308.16	0.3910
20.00	308.21	0.9380
20.00	308.93	0.3220
20.00	309.23	0.9900
20.00	309.65	1.0000
20.00	309.75	0.2470
20.00	312.33	0.1480
20.00	315.65	0.0790
20.00	323.65	0.0000
20.00	307.16	0.8130
101.30	350.44	0.7450
101.30	350.50	0.8100
101.30	350.60	0.6730
101.30	350.83	0.8740
101.30	351.00	0.6060
101.30	351.46	0.9340
101.30	351.57	0.5310
101.30	352.34	0.4550
101.30	352.38	0.9860
101.30	352.68	1.0000
101.30	353.42	0.3790
101.30	354.95	0.2950
101.30	357.33	0.2090
101.30	361.11	0.1320
101.30	365.99	0.0610
101.30	372.33	0.0000

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
0.0300	0.1250
0.0690	0.2290
0.1110	0.3090
0.1520	0.3720
0.2040	0.4450
0.2600	0.4930
0.3130	0.5310
0.3810	0.5670
0.4220	0.5940
0.4770	0.6180
0.5360	0.6490
0.5850	0.6730
0.6360	0.6990
0.6770	0.7260
0.7180	0.7530
0.7890	0.7850
0.8450	0.8250
0.8920	0.8700
0.9430	0.9250
1.0000	1.0000

Azeotropic composition: mole fraction of 2-Butanone (1) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of 2-Butanone (1) - Liquid
101.30	0.7830

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

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Gas	Mole fraction of 2-Butanone (1) - Gas
20.00	306.97	0.7390
20.00	307.03	0.7100
20.00	307.16	0.6840
20.00	307.42	0.6560
20.00	307.55	0.8280
20.00	307.70	0.6370
20.00	308.16	0.6030
20.00	308.21	0.8950
20.00	308.93	0.5760
20.00	309.23	0.9790
20.00	309.65	1.0000
20.00	309.75	0.5350
20.00	312.33	0.4360
20.00	315.65	0.3110
20.00	323.65	0.0000
20.00	307.16	0.7800
101.30	350.44	0.7580
101.30	350.50	0.7970
101.30	350.60	0.7220
101.30	350.83	0.8440
101.30	351.00	0.6890
101.30	351.46	0.9060
101.30	351.57	0.6590
101.30	352.34	0.6240
101.30	352.38	0.9780
101.30	352.68	1.0000
101.30	353.42	0.5870
101.30	354.95	0.5310
101.30	357.33	0.4590
101.30	361.11	0.3580
101.30	365.99	0.2230
101.30	372.33	0.0000

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

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid
20.00	306.97	0.7430
20.00	307.03	0.6730
20.00	307.16	0.6020
20.00	307.42	0.5320
20.00	307.55	0.8810
20.00	307.70	0.4630
20.00	308.16	0.3910
20.00	308.21	0.9380
20.00	308.93	0.3220
20.00	309.23	0.9900
20.00	309.65	1.0000
20.00	309.75	0.2470
20.00	312.33	0.1480
20.00	315.65	0.0790
20.00	323.65	0.0000
20.00	307.16	0.8130
101.30	350.44	0.7450
101.30	350.50	0.8100
101.30	350.60	0.6730
101.30	350.83	0.8740
101.30	351.00	0.6060
101.30	351.46	0.9340
101.30	351.57	0.5310
101.30	352.34	0.4550
101.30	352.38	0.9860
101.30	352.68	1.0000
101.30	353.42	0.3790
101.30	354.95	0.2950
101.30	357.33	0.2090
101.30	361.11	0.1320
101.30	365.99	0.0610
101.30	372.33	0.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0005
298.15	0.0500	0.0005
298.15	0.1000	0.0005
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	0.0004
298.15	0.5000	0.0004
298.15	0.5500	0.0004
298.15	0.6000	0.0004
298.15	0.6500	0.0004
298.15	0.7000	0.0004
298.15	0.7500	0.0004
298.15	0.8000	0.0004
298.15	0.8500	0.0004
298.15	0.9000	0.0004
298.15	0.9500	0.0004
298.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
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	0.0004
308.15	0.6500	0.0004
308.15	0.7000	0.0003
308.15	0.7500	0.0003
308.15	0.8000	0.0003
308.15	0.8500	0.0003
308.15	0.9000	0.0003
308.15	0.9500	0.0003
308.15	1.0000	0.0003
318.15	0.0000	0.0004
318.15	0.0500	0.0004
318.15	0.1000	0.0004
318.15	0.1500	0.0004
318.15	0.2000	0.0004
318.15	0.2500	0.0003
318.15	0.3000	0.0003
318.15	0.3500	0.0003
318.15	0.4000	0.0003
318.15	0.4500	0.0003
318.15	0.5000	0.0003
318.15	0.5500	0.0003
318.15	0.6000	0.0003
318.15	0.6500	0.0003
318.15	0.7000	0.0003
318.15	0.7500	0.0003
318.15	0.8000	0.0003
318.15	0.8500	0.0003
318.15	0.9000	0.0003
318.15	0.9500	0.0003
318.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0005
298.15	0.0500	0.0005
298.15	0.1000	0.0005
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	0.0004
298.15	0.5000	0.0004
298.15	0.5500	0.0004
298.15	0.6000	0.0004
298.15	0.6500	0.0004
298.15	0.7000	0.0004
298.15	0.7500	0.0004
298.15	0.8000	0.0004
298.15	0.8500	0.0004
298.15	0.9000	0.0004
298.15	0.9500	0.0004
298.15	1.0000	0.0004
308.15	0.0000	0.0004
308.15	0.0500	0.0004
308.15	0.1000	0.0004
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	0.0004
308.15	0.6500	0.0004
308.15	0.7000	0.0003
308.15	0.7500	0.0003
308.15	0.8000	0.0003
308.15	0.8500	0.0003
308.15	0.9000	0.0003
308.15	0.9500	0.0003
308.15	1.0000	0.0003
318.15	0.0000	0.0004
318.15	0.0500	0.0004
318.15	0.1000	0.0004
318.15	0.1500	0.0004
318.15	0.2000	0.0004
318.15	0.2500	0.0003
318.15	0.3000	0.0003
318.15	0.3500	0.0003
318.15	0.4000	0.0003
318.15	0.4500	0.0003
318.15	0.5000	0.0003
318.15	0.5500	0.0003
318.15	0.6000	0.0003
318.15	0.6500	0.0003
318.15	0.7000	0.0003
318.15	0.7500	0.0003
318.15	0.8000	0.0003
318.15	0.8500	0.0003
318.15	0.9000	0.0003
318.15	0.9500	0.0003
318.15	1.0000	0.0003

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.8
298.15	0.0500	690.1
298.15	0.1000	692.7
298.15	0.1500	695.6
298.15	0.2000	698.7
298.15	0.2500	702.2
298.15	0.3000	705.9
298.15	0.3500	709.9
298.15	0.4000	714.1
298.15	0.4500	718.7
298.15	0.5000	723.6
298.15	0.5500	728.8
298.15	0.6000	734.5
298.15	0.6500	740.6
298.15	0.7000	747.2
298.15	0.7500	754.2
298.15	0.8000	761.9
298.15	0.8500	770.4
298.15	0.9000	779.3
298.15	0.9500	789.2
298.15	1.0000	799.7
308.15	0.0000	679.5
308.15	0.0500	681.7
308.15	0.1000	684.2
308.15	0.1500	687.0
308.15	0.2000	690.1
308.15	0.2500	693.4
308.15	0.3000	697.0
308.15	0.3500	700.9
308.15	0.4000	705.1
308.15	0.4500	709.5
308.15	0.5000	714.3
308.15	0.5500	719.4
308.15	0.6000	724.9
308.15	0.6500	731.0
308.15	0.7000	737.4
308.15	0.7500	744.3
308.15	0.8000	751.9
308.15	0.8500	760.2
308.15	0.9000	769.0
308.15	0.9500	778.8
308.15	1.0000	789.2
318.15	0.0000	671.0
318.15	0.0500	673.1
318.15	0.1000	675.4
318.15	0.1500	678.2
318.15	0.2000	681.1
318.15	0.2500	684.3
318.15	0.3000	687.8
318.15	0.3500	691.6
318.15	0.4000	695.7
318.15	0.4500	700.1
318.15	0.5000	704.8
318.15	0.5500	709.8
318.15	0.6000	715.3
318.15	0.6500	721.2
318.15	0.7000	727.5
318.15	0.7500	734.3
318.15	0.8000	741.7
318.15	0.8500	749.9
318.15	0.9000	758.6
318.15	0.9500	768.2
318.15	1.0000	778.4

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100.8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	687.8
298.15	0.0500	690.1
298.15	0.1000	692.7
298.15	0.1500	695.6
298.15	0.2000	698.7
298.15	0.2500	702.2
298.15	0.3000	705.9
298.15	0.3500	709.9
298.15	0.4000	714.1
298.15	0.4500	718.7
298.15	0.5000	723.6
298.15	0.5500	728.8
298.15	0.6000	734.5
298.15	0.6500	740.6
298.15	0.7000	747.2
298.15	0.7500	754.2
298.15	0.8000	761.9
298.15	0.8500	770.4
298.15	0.9000	779.3
298.15	0.9500	789.2
298.15	1.0000	799.7
308.15	0.0000	679.5
308.15	0.0500	681.7
308.15	0.1000	684.2
308.15	0.1500	687.0
308.15	0.2000	690.1
308.15	0.2500	693.4
308.15	0.3000	697.0
308.15	0.3500	700.9
308.15	0.4000	705.1
308.15	0.4500	709.5
308.15	0.5000	714.3
308.15	0.5500	719.4
308.15	0.6000	724.9
308.15	0.6500	731.0
308.15	0.7000	737.4
308.15	0.7500	744.3
308.15	0.8000	751.9
308.15	0.8500	760.2
308.15	0.9000	769.0
308.15	0.9500	778.8
308.15	1.0000	789.2
318.15	0.0000	671.0
318.15	0.0500	673.1
318.15	0.1000	675.4
318.15	0.1500	678.2
318.15	0.2000	681.1
318.15	0.2500	684.3
318.15	0.3000	687.8
318.15	0.3500	691.6
318.15	0.4000	695.7
318.15	0.4500	700.1
318.15	0.5000	704.8
318.15	0.5500	709.8
318.15	0.6000	715.3
318.15	0.6500	721.2
318.15	0.7000	727.5
318.15	0.7500	734.3
318.15	0.8000	741.7
318.15	0.8500	749.9
318.15	0.9000	758.6
318.15	0.9500	768.2
318.15	1.0000	778.4

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	372.33
0.0300	368.60
0.0690	364.92
0.1110	362.06
0.1520	359.81
0.2040	357.48
0.2600	355.90
0.3130	354.74
0.3810	353.49
0.4220	352.92
0.4770	352.31
0.5360	351.73
0.5850	351.39
0.6360	351.01
0.6770	350.79
0.7180	350.65
0.7890	350.63
0.8450	350.80
0.8920	351.12
0.9430	351.70
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	372.33
0.0300	368.60
0.0690	364.92
0.1110	362.06
0.1520	359.81
0.2040	357.48
0.2600	355.90
0.3130	354.74
0.3810	353.49
0.4220	352.92
0.4770	352.31
0.5360	351.73
0.5850	351.39
0.6360	351.01
0.6770	350.79
0.7180	350.65
0.7890	350.63
0.8450	350.80
0.8920	351.12
0.9430	351.70
1.0000	352.72

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	350.52

Azeotropic pressure, kPa [ref]

Mole fraction of 2-Butanone (1) - Liquid	Azeotropic pressure, kPa - Liquid
0.7740	20.00
0.7780	101.30

Azeotropic temperature, K [ref]

Mole fraction of 2-Butanone (1) - Liquid	Azeotropic temperature, K - Liquid
0.7740	307.10
0.7780	350.50

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
101.30	350.52

Azeotropic pressure, kPa [ref]

Mole fraction of 2-Butanone (1) - Liquid	Azeotropic pressure, kPa - Liquid
0.7740	20.00
0.7780	101.30

Azeotropic temperature, K [ref]

Mole fraction of 2-Butanone (1) - Liquid	Azeotropic temperature, K - Liquid
0.7740	307.10
0.7780	350.50

Sources

• Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
• Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
• 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