Mixture of 1-Butanol + Ethylene

Datasets

1. Mole fraction (12)
2. P_vap - Vapor or sublimation pressure, kPa (4)
3. ρ_g - Mass density, kg/m3 (4)
4. ρ_l - Mass density, kg/m3 (8)
5. Vapor or sublimation pressure, kPa (2)

Mole fraction of Ethylene (2) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 1
283.65	0.6910

Mole fraction of Ethylene (2) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 2
283.65	0.9730

Mole fraction of Ethylene (2) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of Ethylene (2) - Gas
283.65	0.9990

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (2) - Gas
0.1700	283.65	0.9990
0.2060	290.80	0.9990
0.2240	283.65	0.9950
0.2650	290.80	0.9950
0.3220	283.65	0.9990
0.3390	290.80	0.9970
0.4010	283.65	0.9990
0.4300	290.80	0.9940
0.4700	283.65	0.9990
0.5280	290.80	0.9940
0.5450	283.65	0.9870
0.6220	290.80	0.9960
0.6550	290.80	0.9850
0.6910	290.80	0.9670
0.7450	290.80	0.9320
0.9800	283.65	0.9990
0.9900	283.65	0.9990
0.9940	283.65	0.9990

Mole fraction of Ethylene (2) [ref]

Operational condition: Temperature, K = 283.65 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 1
5379.00	0.7200
5750.00	0.7960

Mole fraction of Ethylene (2) [ref]

Operational condition: Temperature, K = 283.65 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 2
5379.00	0.9370
5750.00	0.9060

Mole fraction of Ethylene (2) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 1
283.65	0.6910

Mole fraction of Ethylene (2) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 2
283.65	0.9730

Mole fraction of Ethylene (2) [ref]

Temperature, K - Liquid mixture 1	Mole fraction of Ethylene (2) - Gas
283.65	0.9990

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (2) - Gas
0.1700	283.65	0.9990
0.2060	290.80	0.9990
0.2240	283.65	0.9950
0.2650	290.80	0.9950
0.3220	283.65	0.9990
0.3390	290.80	0.9970
0.4010	283.65	0.9990
0.4300	290.80	0.9940
0.4700	283.65	0.9990
0.5280	290.80	0.9940
0.5450	283.65	0.9870
0.6220	290.80	0.9960
0.6550	290.80	0.9850
0.6910	290.80	0.9670
0.7450	290.80	0.9320
0.9800	283.65	0.9990
0.9900	283.65	0.9990
0.9940	283.65	0.9990

Mole fraction of Ethylene (2) [ref]

Operational condition: Temperature, K = 283.65 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 1
5379.00	0.7200
5750.00	0.7960

Mole fraction of Ethylene (2) [ref]

Operational condition: Temperature, K = 283.65 (Liquid mixture 1)

Pressure, kPa - Liquid mixture 1	Mole fraction of Ethylene (2) - Liquid mixture 2
5379.00	0.9370
5750.00	0.9060

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 283.65 (Liquid)

Mole fraction of Ethylene (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.8420	5968.00
0.8810	5923.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1700	283.65	1585.00
0.2060	290.80	2104.00
0.2240	283.65	2117.00
0.2650	290.80	2760.00
0.3220	283.65	2912.00
0.3390	290.80	3471.00
0.4010	283.65	3573.00
0.4300	290.80	4195.00
0.4700	283.65	4060.00
0.5280	290.80	5118.00
0.5450	283.65	4588.00
0.6220	290.80	5678.00
0.6550	290.80	5962.00
0.6910	290.80	6278.00
0.7450	290.80	6771.00
0.9800	283.65	5048.00
0.9900	283.65	5069.00
0.9940	283.65	5079.00

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 283.65 (Liquid)

Mole fraction of Ethylene (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.8420	5968.00
0.8810	5923.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1700	283.65	1585.00
0.2060	290.80	2104.00
0.2240	283.65	2117.00
0.2650	290.80	2760.00
0.3220	283.65	2912.00
0.3390	290.80	3471.00
0.4010	283.65	3573.00
0.4300	290.80	4195.00
0.4700	283.65	4060.00
0.5280	290.80	5118.00
0.5450	283.65	4588.00
0.6220	290.80	5678.00
0.6550	290.80	5962.00
0.6910	290.80	6278.00
0.7450	290.80	6771.00
0.9800	283.65	5048.00
0.9900	283.65	5069.00
0.9940	283.65	5079.00

Mass density, kg/m3 [ref]

Mole fraction of Ethylene (2) - Gas	Mass density, kg/m3 - Gas
0.9990	148.7

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Ethylene (2) - Gas	Mass density, kg/m3 - Gas
283.65	0.9870	104.6
283.65	0.9950	31.0
283.65	0.9990	22.6
283.65	0.9990	46.8
283.65	0.9990	62.5
283.65	0.9990	78.0
283.65	0.9990	152.2
283.65	0.9990	159.6
283.65	0.9990	164.9
290.80	0.9320	383.1
290.80	0.9670	332.3
290.80	0.9850	276.6
290.80	0.9940	74.7
290.80	0.9950	41.4
290.80	0.9960	167.6
290.80	0.9970	55.9
290.80	0.9990	29.1
290.80	0.9940	113.4

Mass density, kg/m3 [ref]

Mole fraction of Ethylene (2) - Gas	Mass density, kg/m3 - Gas
0.9990	148.7

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Ethylene (2) - Gas	Mass density, kg/m3 - Gas
283.65	0.9870	104.6
283.65	0.9950	31.0
283.65	0.9990	22.6
283.65	0.9990	46.8
283.65	0.9990	62.5
283.65	0.9990	78.0
283.65	0.9990	152.2
283.65	0.9990	159.6
283.65	0.9990	164.9
290.80	0.9320	383.1
290.80	0.9670	332.3
290.80	0.9850	276.6
290.80	0.9940	74.7
290.80	0.9950	41.4
290.80	0.9960	167.6
290.80	0.9970	55.9
290.80	0.9990	29.1
290.80	0.9940	113.4

Mass density, kg/m3 [ref]

Operational condition: Temperature, K = 283.65 (Liquid)

Mole fraction of Ethylene (2) - Liquid	Mass density, kg/m3 - Liquid
0.8420	489.0
0.8810	446.5

Mass density, kg/m3 [ref]

Mole fraction of Ethylene (2) - Liquid mixture 1	Mass density, kg/m3 - Liquid mixture 1
0.6910	579.7

Mass density, kg/m3 [ref]

Mole fraction of Ethylene (2) - Liquid mixture 2	Mass density, kg/m3 - Liquid mixture 2
0.9730	347.0

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylene (2) - Liquid	Mass density, kg/m3 - Liquid
283.65	0.1700	781.4
283.65	0.2240	767.7
283.65	0.3220	743.7
283.65	0.4010	718.9
283.65	0.4700	695.8
283.65	0.5450	660.9
283.65	0.9800	323.2
283.65	0.9900	296.6
283.65	0.9940	287.0
290.80	0.2060	768.3
290.80	0.2650	752.1
290.80	0.3390	732.0
290.80	0.4300	707.5
290.80	0.5280	664.6
290.80	0.6220	624.4
290.80	0.6550	601.6
290.80	0.6910	585.0
290.80	0.7450	527.5

Mass density, kg/m3 [ref]

Operational condition: Temperature, K = 283.65 (Liquid)

Mole fraction of Ethylene (2) - Liquid	Mass density, kg/m3 - Liquid
0.8420	489.0
0.8810	446.5

Mass density, kg/m3 [ref]

Mole fraction of Ethylene (2) - Liquid mixture 1	Mass density, kg/m3 - Liquid mixture 1
0.6910	579.7

Mass density, kg/m3 [ref]

Mole fraction of Ethylene (2) - Liquid mixture 2	Mass density, kg/m3 - Liquid mixture 2
0.9730	347.0

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylene (2) - Liquid	Mass density, kg/m3 - Liquid
283.65	0.1700	781.4
283.65	0.2240	767.7
283.65	0.3220	743.7
283.65	0.4010	718.9
283.65	0.4700	695.8
283.65	0.5450	660.9
283.65	0.9800	323.2
283.65	0.9900	296.6
283.65	0.9940	287.0
290.80	0.2060	768.3
290.80	0.2650	752.1
290.80	0.3390	732.0
290.80	0.4300	707.5
290.80	0.5280	664.6
290.80	0.6220	624.4
290.80	0.6550	601.6
290.80	0.6910	585.0
290.80	0.7450	527.5

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Gas
283.65	5039.00

Vapor or sublimation pressure, kPa [ref]

Temperature, K - Liquid mixture 1	Vapor or sublimation pressure, kPa - Gas
283.65	5039.00

Sources

• High-pressure phase equilibrium for ethylene + 1-butanol at 283.65 K and 290.80 K