Mixture of Triolein + Methyl Alcohol

Datasets

1. Mole fraction (4)
2. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Methyl Alcohol (2) [ref]

Fixed		Measured
Mole fraction of Methyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0700	10000.00	1.0000
0.1070	8000.00	1.0000
0.1860	6000.00	0.9980
0.3430	10000.00	0.9990
0.4330	8000.00	0.9990
0.5660	6000.00	0.9960
0.5920	8000.00	0.9950
0.5960	10000.00	0.9980
0.6760	6000.00	0.9960
0.6870	10000.00	0.9910
0.6900	8000.00	0.9920
0.7300	6000.00	0.9930
0.7320	8000.00	0.9840
0.7330	8000.00	0.9800
0.7460	6000.00	0.9860
0.7490	6000.00	0.9900
0.7730	10000.00	0.9880
0.7770	6000.00	0.9880
0.7770	10000.00	0.9820
0.7910	8000.00	0.9610
0.8100	10000.00	0.9580

Mole fraction of Methyl Alcohol (2) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
303.15	0.9999
303.15	0.9999
303.15	0.9999
308.15	0.9999
308.15	0.9999
308.15	0.9999
313.15	0.9999
313.15	0.9999
318.15	0.9999
318.15	0.9999
318.15	0.9999
313.15	0.9997
328.15	0.9998
328.15	0.9997
333.15	0.9998
333.15	0.9998

Mole fraction of Methyl Alcohol (2) [ref]

Fixed		Measured
Mole fraction of Methyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0700	10000.00	1.0000
0.1070	8000.00	1.0000
0.1860	6000.00	0.9980
0.3430	10000.00	0.9990
0.4330	8000.00	0.9990
0.5660	6000.00	0.9960
0.5920	8000.00	0.9950
0.5960	10000.00	0.9980
0.6760	6000.00	0.9960
0.6870	10000.00	0.9910
0.6900	8000.00	0.9920
0.7300	6000.00	0.9930
0.7320	8000.00	0.9840
0.7330	8000.00	0.9800
0.7460	6000.00	0.9860
0.7490	6000.00	0.9900
0.7730	10000.00	0.9880
0.7770	6000.00	0.9880
0.7770	10000.00	0.9820
0.7910	8000.00	0.9610
0.8100	10000.00	0.9580

Mole fraction of Methyl Alcohol (2) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Methyl Alcohol (2) - Liquid mixture 1
303.15	0.9999
303.15	0.9999
303.15	0.9999
308.15	0.9999
308.15	0.9999
308.15	0.9999
313.15	0.9999
313.15	0.9999
318.15	0.9999
318.15	0.9999
318.15	0.9999
313.15	0.9997
328.15	0.9998
328.15	0.9997
333.15	0.9998
333.15	0.9998

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Methyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0700	10000.00	353.20
0.1070	8000.00	353.20
0.1860	6000.00	353.20
0.3430	10000.00	393.20
0.4330	8000.00	393.20
0.5660	6000.00	393.20
0.5920	8000.00	413.20
0.5960	10000.00	413.20
0.6760	6000.00	413.20
0.6870	10000.00	433.20
0.6900	8000.00	433.20
0.7300	6000.00	433.20
0.7320	8000.00	443.20
0.7330	8000.00	453.20
0.7460	6000.00	453.20
0.7490	6000.00	443.20
0.7730	10000.00	443.20
0.7770	6000.00	463.20
0.7770	10000.00	453.20
0.7910	8000.00	463.20
0.8100	10000.00	463.20

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Methyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0700	10000.00	353.20
0.1070	8000.00	353.20
0.1860	6000.00	353.20
0.3430	10000.00	393.20
0.4330	8000.00	393.20
0.5660	6000.00	393.20
0.5920	8000.00	413.20
0.5960	10000.00	413.20
0.6760	6000.00	413.20
0.6870	10000.00	433.20
0.6900	8000.00	433.20
0.7300	6000.00	433.20
0.7320	8000.00	443.20
0.7330	8000.00	453.20
0.7460	6000.00	453.20
0.7490	6000.00	443.20
0.7730	10000.00	443.20
0.7770	6000.00	463.20
0.7770	10000.00	453.20
0.7910	8000.00	463.20
0.8100	10000.00	463.20

Sources

• Phase equilibria of methanol triolein system at elevated temperature and pressure
• Phase equilibria of triolein to biodiesel reactor systems