Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid mixture 1 |
---|---|
299.70 | 0.0420 |
304.90 | 0.0370 |
310.90 | 0.0320 |
316.60 | 0.0330 |
320.20 | 0.0500 |
331.80 | 0.0310 |
340.70 | 0.0790 |
Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid mixture 2 |
---|---|
299.70 | 0.8760 |
304.90 | 0.8730 |
310.90 | 0.8520 |
316.60 | 0.8140 |
320.20 | 0.8060 |
331.80 | 0.7530 |
340.70 | 0.7930 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid | Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Gas |
---|---|
0.8230 | 0.6250 |
0.8050 | 0.6670 |
0.7630 | 0.6530 |
0.7540 | 0.5280 |
0.5380 | 0.6090 |
0.1900 | 0.5530 |
0.9250 | 0.6310 |
0.0150 | 0.5200 |
0.0060 | 0.4360 |
0.0340 | 0.5090 |
0.9600 | 0.7250 |
0.0100 | 0.3000 |
0.0040 | 0.2390 |
0.0030 | 0.1600 |
0.9850 | 0.9000 |
1.0000 | 1.0000 |
0.0030 | 0.0750 |
0.0100 | 0.0650 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid mixture 1 |
---|---|
299.70 | 0.0420 |
304.90 | 0.0370 |
310.90 | 0.0320 |
316.60 | 0.0330 |
320.20 | 0.0500 |
331.80 | 0.0310 |
340.70 | 0.0790 |
Operational condition: Pressure, kPa = 99 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid mixture 2 |
---|---|
299.70 | 0.8760 |
304.90 | 0.8730 |
310.90 | 0.8520 |
316.60 | 0.8140 |
320.20 | 0.8060 |
331.80 | 0.7530 |
340.70 | 0.7930 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid | Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Gas |
---|---|
0.8230 | 0.6250 |
0.8050 | 0.6670 |
0.7630 | 0.6530 |
0.7540 | 0.5280 |
0.5380 | 0.6090 |
0.1900 | 0.5530 |
0.9250 | 0.6310 |
0.0150 | 0.5200 |
0.0060 | 0.4360 |
0.0340 | 0.5090 |
0.9600 | 0.7250 |
0.0100 | 0.3000 |
0.0040 | 0.2390 |
0.0030 | 0.1600 |
0.9850 | 0.9000 |
1.0000 | 1.0000 |
0.0030 | 0.0750 |
0.0100 | 0.0650 |
0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.8230 | 352.10 |
0.8050 | 352.10 |
0.7630 | 352.10 |
0.7540 | 352.10 |
0.5380 | 352.10 |
0.1900 | 352.10 |
0.9250 | 352.50 |
0.0150 | 353.00 |
0.0060 | 355.20 |
0.0340 | 357.40 |
0.9600 | 358.00 |
0.0100 | 358.00 |
0.0040 | 359.30 |
0.0030 | 363.00 |
0.9850 | 363.00 |
1.0000 | 366.00 |
0.0030 | 368.00 |
0.0100 | 371.80 |
0.0000 | 373.00 |
Operational condition: Pressure, kPa = 99 (Liquid)
Mole fraction of 1,3-Dioxolane, 2,4-dimethyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.8230 | 352.10 |
0.8050 | 352.10 |
0.7630 | 352.10 |
0.7540 | 352.10 |
0.5380 | 352.10 |
0.1900 | 352.10 |
0.9250 | 352.50 |
0.0150 | 353.00 |
0.0060 | 355.20 |
0.0340 | 357.40 |
0.9600 | 358.00 |
0.0100 | 358.00 |
0.0040 | 359.30 |
0.0030 | 363.00 |
0.9850 | 363.00 |
1.0000 | 366.00 |
0.0030 | 368.00 |
0.0100 | 371.80 |
0.0000 | 373.00 |