Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid mixture 1 |
---|---|
295.70 | 0.0740 |
303.80 | 0.0770 |
307.80 | 0.0830 |
312.60 | 0.0890 |
319.40 | 0.0950 |
324.20 | 0.1050 |
330.00 | 0.1170 |
336.50 | 0.1200 |
342.60 | 0.1230 |
Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid mixture 2 |
---|---|
295.70 | 0.6160 |
303.80 | 0.6100 |
307.80 | 0.6070 |
312.60 | 0.6000 |
319.40 | 0.5950 |
324.20 | 0.5900 |
330.00 | 0.5850 |
336.50 | 0.5820 |
342.60 | 0.5800 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid | Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Gas |
---|---|
0.1130 | 0.6090 |
0.6480 | 0.6320 |
0.1380 | 0.5730 |
0.7440 | 0.6940 |
0.5770 | 0.6730 |
0.5400 | 0.6220 |
0.4700 | 0.6170 |
0.2680 | 0.6800 |
0.2320 | 0.6610 |
0.1960 | 0.6010 |
0.4220 | 0.6740 |
0.4070 | 0.6740 |
0.3330 | 0.6720 |
0.7740 | 0.8160 |
0.9180 | 0.8630 |
0.9620 | 0.9220 |
0.0170 | 0.4490 |
1.0000 | 1.0000 |
0.0080 | 0.2560 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid mixture 1 |
---|---|
295.70 | 0.0740 |
303.80 | 0.0770 |
307.80 | 0.0830 |
312.60 | 0.0890 |
319.40 | 0.0950 |
324.20 | 0.1050 |
330.00 | 0.1170 |
336.50 | 0.1200 |
342.60 | 0.1230 |
Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid mixture 2 |
---|---|
295.70 | 0.6160 |
303.80 | 0.6100 |
307.80 | 0.6070 |
312.60 | 0.6000 |
319.40 | 0.5950 |
324.20 | 0.5900 |
330.00 | 0.5850 |
336.50 | 0.5820 |
342.60 | 0.5800 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid | Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Gas |
---|---|
0.1130 | 0.6090 |
0.6480 | 0.6320 |
0.1380 | 0.5730 |
0.7440 | 0.6940 |
0.5770 | 0.6730 |
0.5400 | 0.6220 |
0.4700 | 0.6170 |
0.2680 | 0.6800 |
0.2320 | 0.6610 |
0.1960 | 0.6010 |
0.4220 | 0.6740 |
0.4070 | 0.6740 |
0.3330 | 0.6720 |
0.7740 | 0.8160 |
0.9180 | 0.8630 |
0.9620 | 0.9220 |
0.0170 | 0.4490 |
1.0000 | 1.0000 |
0.0080 | 0.2560 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.1130 | 348.10 |
0.6480 | 348.20 |
0.1380 | 348.20 |
0.7440 | 348.30 |
0.5770 | 348.30 |
0.5400 | 348.30 |
0.4700 | 348.30 |
0.2680 | 348.30 |
0.2320 | 348.30 |
0.1960 | 348.30 |
0.4220 | 348.40 |
0.4070 | 348.40 |
0.3330 | 348.40 |
0.7740 | 349.40 |
0.9180 | 350.40 |
0.9620 | 352.70 |
0.0170 | 355.80 |
1.0000 | 356.00 |
0.0080 | 364.50 |
0.0000 | 373.00 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.1130 | 348.10 |
0.6480 | 348.20 |
0.1380 | 348.20 |
0.7440 | 348.30 |
0.5770 | 348.30 |
0.5400 | 348.30 |
0.4700 | 348.30 |
0.2680 | 348.30 |
0.2320 | 348.30 |
0.1960 | 348.30 |
0.4220 | 348.40 |
0.4070 | 348.40 |
0.3330 | 348.40 |
0.7740 | 349.40 |
0.9180 | 350.40 |
0.9620 | 352.70 |
0.0170 | 355.80 |
1.0000 | 356.00 |
0.0080 | 364.50 |
0.0000 | 373.00 |