Mixture of Diethyl carbonate + Ethyl Acetate
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Ethyl Acetate (2)
[ref]
Fixed |
Measured |
Mole fraction of Ethyl Acetate (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
0.0770 |
373.20 |
0.2510 |
0.1570 |
373.20 |
0.4000 |
0.2580 |
373.20 |
0.5910 |
0.4090 |
373.20 |
0.7660 |
0.5540 |
373.20 |
0.8590 |
0.6820 |
373.20 |
0.9130 |
0.8250 |
373.20 |
0.9530 |
0.8880 |
373.20 |
0.9700 |
0.1000 |
413.20 |
0.2860 |
0.1560 |
413.20 |
0.4390 |
0.2850 |
413.20 |
0.5330 |
0.3650 |
413.20 |
0.6320 |
0.4400 |
413.20 |
0.7100 |
0.5510 |
413.20 |
0.7890 |
0.6830 |
413.20 |
0.8780 |
0.8260 |
413.20 |
0.9420 |
0.0980 |
453.20 |
0.2450 |
0.1700 |
453.20 |
0.3630 |
0.2680 |
453.20 |
0.4850 |
0.3990 |
453.20 |
0.6090 |
0.5420 |
453.20 |
0.7320 |
0.6620 |
453.20 |
0.8600 |
0.8030 |
453.20 |
0.9180 |
Mole fraction of Ethyl Acetate (2)
[ref]
Fixed |
Measured |
Mole fraction of Ethyl Acetate (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
0.0770 |
373.20 |
0.2510 |
0.1570 |
373.20 |
0.4000 |
0.2580 |
373.20 |
0.5910 |
0.4090 |
373.20 |
0.7660 |
0.5540 |
373.20 |
0.8590 |
0.6820 |
373.20 |
0.9130 |
0.8250 |
373.20 |
0.9530 |
0.8880 |
373.20 |
0.9700 |
0.1000 |
413.20 |
0.2860 |
0.1560 |
413.20 |
0.4390 |
0.2850 |
413.20 |
0.5330 |
0.3650 |
413.20 |
0.6320 |
0.4400 |
413.20 |
0.7100 |
0.5510 |
413.20 |
0.7890 |
0.6830 |
413.20 |
0.8780 |
0.8260 |
413.20 |
0.9420 |
0.0980 |
453.20 |
0.2450 |
0.1700 |
453.20 |
0.3630 |
0.2680 |
453.20 |
0.4850 |
0.3990 |
453.20 |
0.6090 |
0.5420 |
453.20 |
0.7320 |
0.6620 |
453.20 |
0.8600 |
0.8030 |
453.20 |
0.9180 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethyl Acetate (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0770 |
373.20 |
53.90 |
0.1570 |
373.20 |
65.90 |
0.2580 |
373.20 |
80.50 |
0.4090 |
373.20 |
104.70 |
0.5540 |
373.20 |
130.60 |
0.6820 |
373.20 |
155.20 |
0.8250 |
373.20 |
179.40 |
0.8880 |
373.20 |
188.00 |
0.1000 |
413.20 |
193.10 |
0.1560 |
413.20 |
220.00 |
0.2850 |
413.20 |
252.90 |
0.3650 |
413.20 |
288.70 |
0.4400 |
413.20 |
314.20 |
0.5510 |
413.20 |
362.80 |
0.6830 |
413.20 |
418.90 |
0.8260 |
413.20 |
473.40 |
0.0980 |
453.20 |
461.70 |
0.1700 |
453.20 |
518.60 |
0.2680 |
453.20 |
568.90 |
0.3990 |
453.20 |
680.50 |
0.5420 |
453.20 |
803.20 |
0.6620 |
453.20 |
915.90 |
0.8030 |
453.20 |
1052.90 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Ethyl Acetate (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0770 |
373.20 |
53.90 |
0.1570 |
373.20 |
65.90 |
0.2580 |
373.20 |
80.50 |
0.4090 |
373.20 |
104.70 |
0.5540 |
373.20 |
130.60 |
0.6820 |
373.20 |
155.20 |
0.8250 |
373.20 |
179.40 |
0.8880 |
373.20 |
188.00 |
0.1000 |
413.20 |
193.10 |
0.1560 |
413.20 |
220.00 |
0.2850 |
413.20 |
252.90 |
0.3650 |
413.20 |
288.70 |
0.4400 |
413.20 |
314.20 |
0.5510 |
413.20 |
362.80 |
0.6830 |
413.20 |
418.90 |
0.8260 |
413.20 |
473.40 |
0.0980 |
453.20 |
461.70 |
0.1700 |
453.20 |
518.60 |
0.2680 |
453.20 |
568.90 |
0.3990 |
453.20 |
680.50 |
0.5420 |
453.20 |
803.20 |
0.6620 |
453.20 |
915.90 |
0.8030 |
453.20 |
1052.90 |
Sources