Mixture of Carbonic acid, dibutyl ester + 1-Butanol
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 1-Butanol (2)
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1-Butanol (2) - Gas |
0.0000 |
40.00 |
0.0000 |
0.0340 |
40.00 |
0.2780 |
0.0860 |
40.00 |
0.5230 |
0.1130 |
40.00 |
0.6020 |
0.2020 |
40.00 |
0.7650 |
0.3340 |
40.00 |
0.8780 |
0.4130 |
40.00 |
0.9130 |
0.4890 |
40.00 |
0.9420 |
0.5760 |
40.00 |
0.9610 |
0.6550 |
40.00 |
0.9780 |
0.7430 |
40.00 |
0.9850 |
0.8060 |
40.00 |
0.9910 |
0.9260 |
40.00 |
0.9970 |
1.0000 |
40.00 |
1.0000 |
0.0000 |
70.00 |
0.0000 |
0.0280 |
70.00 |
0.2340 |
0.0890 |
70.00 |
0.5250 |
0.1260 |
70.00 |
0.6280 |
0.2030 |
70.00 |
0.7610 |
0.2820 |
70.00 |
0.8410 |
0.3640 |
70.00 |
0.8890 |
0.4080 |
70.00 |
0.9100 |
0.5460 |
70.00 |
0.9530 |
0.6540 |
70.00 |
0.9720 |
0.7020 |
70.00 |
0.9810 |
0.7730 |
70.00 |
0.9870 |
0.9130 |
70.00 |
0.9950 |
1.0000 |
70.00 |
1.0000 |
0.0000 |
100.00 |
0.0000 |
0.0420 |
100.00 |
0.2920 |
0.1250 |
100.00 |
0.5940 |
0.1690 |
100.00 |
0.6850 |
0.2440 |
100.00 |
0.7840 |
0.3220 |
100.00 |
0.8580 |
0.4020 |
100.00 |
0.9020 |
0.4450 |
100.00 |
0.9180 |
0.5720 |
100.00 |
0.9550 |
0.6650 |
100.00 |
0.9700 |
0.7260 |
100.00 |
0.9780 |
0.7930 |
100.00 |
0.9850 |
0.8960 |
100.00 |
0.9930 |
1.0000 |
100.00 |
1.0000 |
Mole fraction of 1-Butanol (2)
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 1-Butanol (2) - Gas |
0.0000 |
40.00 |
0.0000 |
0.0340 |
40.00 |
0.2780 |
0.0860 |
40.00 |
0.5230 |
0.1130 |
40.00 |
0.6020 |
0.2020 |
40.00 |
0.7650 |
0.3340 |
40.00 |
0.8780 |
0.4130 |
40.00 |
0.9130 |
0.4890 |
40.00 |
0.9420 |
0.5760 |
40.00 |
0.9610 |
0.6550 |
40.00 |
0.9780 |
0.7430 |
40.00 |
0.9850 |
0.8060 |
40.00 |
0.9910 |
0.9260 |
40.00 |
0.9970 |
1.0000 |
40.00 |
1.0000 |
0.0000 |
70.00 |
0.0000 |
0.0280 |
70.00 |
0.2340 |
0.0890 |
70.00 |
0.5250 |
0.1260 |
70.00 |
0.6280 |
0.2030 |
70.00 |
0.7610 |
0.2820 |
70.00 |
0.8410 |
0.3640 |
70.00 |
0.8890 |
0.4080 |
70.00 |
0.9100 |
0.5460 |
70.00 |
0.9530 |
0.6540 |
70.00 |
0.9720 |
0.7020 |
70.00 |
0.9810 |
0.7730 |
70.00 |
0.9870 |
0.9130 |
70.00 |
0.9950 |
1.0000 |
70.00 |
1.0000 |
0.0000 |
100.00 |
0.0000 |
0.0420 |
100.00 |
0.2920 |
0.1250 |
100.00 |
0.5940 |
0.1690 |
100.00 |
0.6850 |
0.2440 |
100.00 |
0.7840 |
0.3220 |
100.00 |
0.8580 |
0.4020 |
100.00 |
0.9020 |
0.4450 |
100.00 |
0.9180 |
0.5720 |
100.00 |
0.9550 |
0.6650 |
100.00 |
0.9700 |
0.7260 |
100.00 |
0.9780 |
0.7930 |
100.00 |
0.9850 |
0.8960 |
100.00 |
0.9930 |
1.0000 |
100.00 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
40.00 |
443.78 |
0.0340 |
40.00 |
434.24 |
0.0860 |
40.00 |
423.24 |
0.1130 |
40.00 |
418.54 |
0.2020 |
40.00 |
406.73 |
0.3340 |
40.00 |
394.82 |
0.4130 |
40.00 |
389.47 |
0.4890 |
40.00 |
385.20 |
0.5760 |
40.00 |
380.89 |
0.6550 |
40.00 |
377.62 |
0.7430 |
40.00 |
374.26 |
0.8060 |
40.00 |
372.17 |
0.9260 |
40.00 |
368.79 |
1.0000 |
40.00 |
367.03 |
0.0000 |
70.00 |
464.01 |
0.0280 |
70.00 |
455.48 |
0.0890 |
70.00 |
440.98 |
0.1260 |
70.00 |
434.52 |
0.2030 |
70.00 |
423.65 |
0.2820 |
70.00 |
415.56 |
0.3640 |
70.00 |
408.62 |
0.4080 |
70.00 |
405.48 |
0.5460 |
70.00 |
397.48 |
0.6540 |
70.00 |
392.45 |
0.7020 |
70.00 |
390.72 |
0.7730 |
70.00 |
387.82 |
0.9130 |
70.00 |
383.48 |
1.0000 |
70.00 |
381.07 |
0.0000 |
100.00 |
478.02 |
0.0420 |
100.00 |
465.66 |
0.1250 |
100.00 |
448.22 |
0.1690 |
100.00 |
441.31 |
0.2440 |
100.00 |
431.96 |
0.3220 |
100.00 |
424.38 |
0.4020 |
100.00 |
417.84 |
0.4450 |
100.00 |
414.82 |
0.5720 |
100.00 |
407.17 |
0.6650 |
100.00 |
402.65 |
0.7260 |
100.00 |
399.95 |
0.7930 |
100.00 |
397.35 |
0.8960 |
100.00 |
393.77 |
1.0000 |
100.00 |
390.78 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 1-Butanol (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
40.00 |
443.78 |
0.0340 |
40.00 |
434.24 |
0.0860 |
40.00 |
423.24 |
0.1130 |
40.00 |
418.54 |
0.2020 |
40.00 |
406.73 |
0.3340 |
40.00 |
394.82 |
0.4130 |
40.00 |
389.47 |
0.4890 |
40.00 |
385.20 |
0.5760 |
40.00 |
380.89 |
0.6550 |
40.00 |
377.62 |
0.7430 |
40.00 |
374.26 |
0.8060 |
40.00 |
372.17 |
0.9260 |
40.00 |
368.79 |
1.0000 |
40.00 |
367.03 |
0.0000 |
70.00 |
464.01 |
0.0280 |
70.00 |
455.48 |
0.0890 |
70.00 |
440.98 |
0.1260 |
70.00 |
434.52 |
0.2030 |
70.00 |
423.65 |
0.2820 |
70.00 |
415.56 |
0.3640 |
70.00 |
408.62 |
0.4080 |
70.00 |
405.48 |
0.5460 |
70.00 |
397.48 |
0.6540 |
70.00 |
392.45 |
0.7020 |
70.00 |
390.72 |
0.7730 |
70.00 |
387.82 |
0.9130 |
70.00 |
383.48 |
1.0000 |
70.00 |
381.07 |
0.0000 |
100.00 |
478.02 |
0.0420 |
100.00 |
465.66 |
0.1250 |
100.00 |
448.22 |
0.1690 |
100.00 |
441.31 |
0.2440 |
100.00 |
431.96 |
0.3220 |
100.00 |
424.38 |
0.4020 |
100.00 |
417.84 |
0.4450 |
100.00 |
414.82 |
0.5720 |
100.00 |
407.17 |
0.6650 |
100.00 |
402.65 |
0.7260 |
100.00 |
399.95 |
0.7930 |
100.00 |
397.35 |
0.8960 |
100.00 |
393.77 |
1.0000 |
100.00 |
390.78 |
Sources