Mixture of 1-Dodecanol + Ethanol + Water

Datasets

1. Mole fraction (12)

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
281.10	0.4440
288.15	0.1690
296.15	0.0192

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Ethanol (2) - Liquid mixture 2
281.10	0.3550
288.15	0.0664
296.15	0.0054

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1
281.10	0.5470
288.15	0.8310
296.15	0.9810

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
281.10	0.1490
288.15	0.0434
296.15	0.0225

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
278.10	0.0000	0.3930
278.10	0.0390	0.4000
278.10	0.0880	0.4160
278.10	0.1470	0.4360
278.10	0.1970	0.4620
278.10	0.2420	0.4740
278.10	0.2760	0.4860
278.10	0.3100	0.4920
278.10	0.3510	0.5000
278.10	0.3960	0.5070
278.10	0.4410	0.5000
278.10	0.4930	0.4850
278.10	0.5140	0.4750
278.10	0.5470	0.4480
278.10	0.5780	0.4190
281.10	0.1130	0.3220
281.10	0.1600	0.3710
281.10	0.2060	0.4090
281.10	0.2550	0.4370
281.10	0.3300	0.4750
281.10	0.4070	0.4890
281.10	0.5040	0.4760
288.15	0.0500	0.1160
288.15	0.0550	0.1660
288.15	0.0690	0.2060
288.15	0.0830	0.2490
288.15	0.1100	0.2900
288.15	0.1380	0.3230
288.15	0.1610	0.3500
288.15	0.1890	0.3790
288.15	0.2330	0.4050
288.15	0.2780	0.4250
288.15	0.3190	0.4500
288.15	0.3500	0.4660
288.15	0.4220	0.4690
288.15	0.4740	0.4740
288.15	0.5030	0.4750
288.15	0.5270	0.4610
288.15	0.5400	0.4520
288.15	0.5740	0.4210
296.15	0.0260	0.0250
296.15	0.0600	0.1580
296.15	0.1080	0.2680
296.15	0.1940	0.3620
296.15	0.2390	0.4080
296.15	0.2870	0.4240
296.15	0.3760	0.4480
296.15	0.4630	0.4610
296.15	0.5550	0.4270
303.15	0.0210	0.0000
303.15	0.0290	0.0440
303.15	0.0310	0.0150
303.15	0.0320	0.1170
303.15	0.0330	0.0700
303.15	0.0380	0.1390
303.15	0.0610	0.1830
303.15	0.0730	0.2250
303.15	0.1070	0.2960
303.15	0.1480	0.3530
303.15	0.2960	0.4250
303.15	0.3560	0.4440
303.15	0.4100	0.4590
303.15	0.4720	0.4640
303.15	0.5040	0.4560
303.15	0.5080	0.4560
303.15	0.5880	0.4080
303.15	0.6130	0.3840
303.15	0.6360	0.3620

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 2	Mole fraction of Ethanol (2) - Liquid mixture 2
288.15	0.5260	0.4610	0.1780	0.3660
288.15	0.6350	0.3650	0.0840	0.2450
288.15	0.7340	0.2660	0.0520	0.1380
288.15	0.7970	0.2030	0.0460	0.0960
296.15	0.5590	0.4210	0.1540	0.3300
296.15	0.6340	0.3630	0.1020	0.2560
296.15	0.7370	0.2630	0.0580	0.1510
296.15	0.8600	0.1400	0.0340	0.0630
296.15	0.9610	0.0390	0.0240	0.0150
303.15	0.5270	0.4460	0.2140	0.3830
303.15	0.6510	0.3490	0.0850	0.2570
303.15	0.7600	0.2440	0.0490	0.1630
303.15	0.8730	0.1270	0.0320	0.0740
303.15	1.0000	0.0000	0.0280	0.0000

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
281.10	0.4440
288.15	0.1690
296.15	0.0192

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Ethanol (2) - Liquid mixture 2
281.10	0.3550
288.15	0.0664
296.15	0.0054

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1
281.10	0.5470
288.15	0.8310
296.15	0.9810

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Water (3) - Liquid mixture 2
281.10	0.1490
288.15	0.0434
296.15	0.0225

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
278.10	0.0000	0.3930
278.10	0.0390	0.4000
278.10	0.0880	0.4160
278.10	0.1470	0.4360
278.10	0.1970	0.4620
278.10	0.2420	0.4740
278.10	0.2760	0.4860
278.10	0.3100	0.4920
278.10	0.3510	0.5000
278.10	0.3960	0.5070
278.10	0.4410	0.5000
278.10	0.4930	0.4850
278.10	0.5140	0.4750
278.10	0.5470	0.4480
278.10	0.5780	0.4190
281.10	0.1130	0.3220
281.10	0.1600	0.3710
281.10	0.2060	0.4090
281.10	0.2550	0.4370
281.10	0.3300	0.4750
281.10	0.4070	0.4890
281.10	0.5040	0.4760
288.15	0.0500	0.1160
288.15	0.0550	0.1660
288.15	0.0690	0.2060
288.15	0.0830	0.2490
288.15	0.1100	0.2900
288.15	0.1380	0.3230
288.15	0.1610	0.3500
288.15	0.1890	0.3790
288.15	0.2330	0.4050
288.15	0.2780	0.4250
288.15	0.3190	0.4500
288.15	0.3500	0.4660
288.15	0.4220	0.4690
288.15	0.4740	0.4740
288.15	0.5030	0.4750
288.15	0.5270	0.4610
288.15	0.5400	0.4520
288.15	0.5740	0.4210
296.15	0.0260	0.0250
296.15	0.0600	0.1580
296.15	0.1080	0.2680
296.15	0.1940	0.3620
296.15	0.2390	0.4080
296.15	0.2870	0.4240
296.15	0.3760	0.4480
296.15	0.4630	0.4610
296.15	0.5550	0.4270
303.15	0.0210	0.0000
303.15	0.0290	0.0440
303.15	0.0310	0.0150
303.15	0.0320	0.1170
303.15	0.0330	0.0700
303.15	0.0380	0.1390
303.15	0.0610	0.1830
303.15	0.0730	0.2250
303.15	0.1070	0.2960
303.15	0.1480	0.3530
303.15	0.2960	0.4250
303.15	0.3560	0.4440
303.15	0.4100	0.4590
303.15	0.4720	0.4640
303.15	0.5040	0.4560
303.15	0.5080	0.4560
303.15	0.5880	0.4080
303.15	0.6130	0.3840
303.15	0.6360	0.3620

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 2	Mole fraction of Ethanol (2) - Liquid mixture 2
288.15	0.5260	0.4610	0.1780	0.3660
288.15	0.6350	0.3650	0.0840	0.2450
288.15	0.7340	0.2660	0.0520	0.1380
288.15	0.7970	0.2030	0.0460	0.0960
296.15	0.5590	0.4210	0.1540	0.3300
296.15	0.6340	0.3630	0.1020	0.2560
296.15	0.7370	0.2630	0.0580	0.1510
296.15	0.8600	0.1400	0.0340	0.0630
296.15	0.9610	0.0390	0.0240	0.0150
303.15	0.5270	0.4460	0.2140	0.3830
303.15	0.6510	0.3490	0.0850	0.2570
303.15	0.7600	0.2440	0.0490	0.1630
303.15	0.8730	0.1270	0.0320	0.0740
303.15	1.0000	0.0000	0.0280	0.0000

Sources

• The influence of temperature on the liquid liquid solid equilibria of the ternary system water + ethanol + 1-dodecanol