Datasets
-
Mole fraction (4)
-
ρl - Mass density, kg/m3 (2)
-
Tboil - Boiling temperature at pressure P, K (4)
-
Vapor Liquid Equilibrium at Constant Pressure (3)
Mole fraction of Isopropyl Alcohol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Gas |
0.9102 |
0.9738 |
0.7426 |
0.9167 |
0.6093 |
0.8602 |
0.4600 |
0.7987 |
0.3704 |
0.7417 |
0.2893 |
0.6711 |
0.2151 |
0.5908 |
0.1834 |
0.5472 |
0.1293 |
0.4478 |
0.1004 |
0.3851 |
0.0795 |
0.3316 |
0.0381 |
0.1880 |
0.0204 |
0.1151 |
Mole fraction of Acetic acid, butyl ester (2)
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Acetic acid, butyl ester (2) - Gas |
0.0000 |
150.00 |
0.0000 |
0.0140 |
150.00 |
0.0040 |
0.0200 |
150.00 |
0.0090 |
0.0500 |
150.00 |
0.0240 |
0.0870 |
150.00 |
0.0370 |
0.1120 |
150.00 |
0.0460 |
0.1370 |
150.00 |
0.0570 |
0.1700 |
150.00 |
0.0660 |
0.2000 |
150.00 |
0.0770 |
0.2270 |
150.00 |
0.0840 |
0.2530 |
150.00 |
0.0930 |
0.2850 |
150.00 |
0.1000 |
0.3100 |
150.00 |
0.1100 |
0.3380 |
150.00 |
0.1190 |
0.3660 |
150.00 |
0.1280 |
0.3980 |
150.00 |
0.1430 |
0.4310 |
150.00 |
0.1580 |
0.4590 |
150.00 |
0.1680 |
0.4950 |
150.00 |
0.1880 |
0.5330 |
150.00 |
0.2020 |
0.5500 |
150.00 |
0.2130 |
0.5740 |
150.00 |
0.2270 |
0.5950 |
150.00 |
0.2400 |
0.6830 |
150.00 |
0.2930 |
0.7070 |
150.00 |
0.3140 |
0.7860 |
150.00 |
0.3780 |
0.8580 |
150.00 |
0.4610 |
0.9160 |
150.00 |
0.6140 |
0.9510 |
150.00 |
0.7240 |
0.9730 |
150.00 |
0.8370 |
0.9810 |
150.00 |
0.8830 |
1.0000 |
150.00 |
1.0000 |
0.0000 |
600.00 |
0.0000 |
0.0150 |
600.00 |
0.0050 |
0.0400 |
600.00 |
0.0140 |
0.0690 |
600.00 |
0.0260 |
0.1010 |
600.00 |
0.0370 |
0.1510 |
600.00 |
0.0530 |
0.1750 |
600.00 |
0.0610 |
0.2010 |
600.00 |
0.0710 |
0.2360 |
600.00 |
0.0810 |
0.2550 |
600.00 |
0.0910 |
0.2760 |
600.00 |
0.0980 |
0.3080 |
600.00 |
0.1100 |
0.3260 |
600.00 |
0.1190 |
0.3590 |
600.00 |
0.1320 |
0.3790 |
600.00 |
0.1430 |
0.4050 |
600.00 |
0.1540 |
0.4880 |
600.00 |
0.1960 |
0.5200 |
600.00 |
0.2220 |
0.5770 |
600.00 |
0.2500 |
0.6650 |
600.00 |
0.3210 |
0.7170 |
600.00 |
0.3620 |
0.7770 |
600.00 |
0.4390 |
0.8270 |
600.00 |
0.4980 |
0.8540 |
600.00 |
0.5390 |
0.9160 |
600.00 |
0.7080 |
0.9760 |
600.00 |
0.8930 |
0.9840 |
600.00 |
0.9330 |
0.9910 |
600.00 |
0.9640 |
1.0000 |
600.00 |
1.0000 |
Mole fraction of Isopropyl Alcohol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Gas |
0.9102 |
0.9738 |
0.7426 |
0.9167 |
0.6093 |
0.8602 |
0.4600 |
0.7987 |
0.3704 |
0.7417 |
0.2893 |
0.6711 |
0.2151 |
0.5908 |
0.1834 |
0.5472 |
0.1293 |
0.4478 |
0.1004 |
0.3851 |
0.0795 |
0.3316 |
0.0381 |
0.1880 |
0.0204 |
0.1151 |
Mole fraction of Acetic acid, butyl ester (2)
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Acetic acid, butyl ester (2) - Gas |
0.0000 |
150.00 |
0.0000 |
0.0140 |
150.00 |
0.0040 |
0.0200 |
150.00 |
0.0090 |
0.0500 |
150.00 |
0.0240 |
0.0870 |
150.00 |
0.0370 |
0.1120 |
150.00 |
0.0460 |
0.1370 |
150.00 |
0.0570 |
0.1700 |
150.00 |
0.0660 |
0.2000 |
150.00 |
0.0770 |
0.2270 |
150.00 |
0.0840 |
0.2530 |
150.00 |
0.0930 |
0.2850 |
150.00 |
0.1000 |
0.3100 |
150.00 |
0.1100 |
0.3380 |
150.00 |
0.1190 |
0.3660 |
150.00 |
0.1280 |
0.3980 |
150.00 |
0.1430 |
0.4310 |
150.00 |
0.1580 |
0.4590 |
150.00 |
0.1680 |
0.4950 |
150.00 |
0.1880 |
0.5330 |
150.00 |
0.2020 |
0.5500 |
150.00 |
0.2130 |
0.5740 |
150.00 |
0.2270 |
0.5950 |
150.00 |
0.2400 |
0.6830 |
150.00 |
0.2930 |
0.7070 |
150.00 |
0.3140 |
0.7860 |
150.00 |
0.3780 |
0.8580 |
150.00 |
0.4610 |
0.9160 |
150.00 |
0.6140 |
0.9510 |
150.00 |
0.7240 |
0.9730 |
150.00 |
0.8370 |
0.9810 |
150.00 |
0.8830 |
1.0000 |
150.00 |
1.0000 |
0.0000 |
600.00 |
0.0000 |
0.0150 |
600.00 |
0.0050 |
0.0400 |
600.00 |
0.0140 |
0.0690 |
600.00 |
0.0260 |
0.1010 |
600.00 |
0.0370 |
0.1510 |
600.00 |
0.0530 |
0.1750 |
600.00 |
0.0610 |
0.2010 |
600.00 |
0.0710 |
0.2360 |
600.00 |
0.0810 |
0.2550 |
600.00 |
0.0910 |
0.2760 |
600.00 |
0.0980 |
0.3080 |
600.00 |
0.1100 |
0.3260 |
600.00 |
0.1190 |
0.3590 |
600.00 |
0.1320 |
0.3790 |
600.00 |
0.1430 |
0.4050 |
600.00 |
0.1540 |
0.4880 |
600.00 |
0.1960 |
0.5200 |
600.00 |
0.2220 |
0.5770 |
600.00 |
0.2500 |
0.6650 |
600.00 |
0.3210 |
0.7170 |
600.00 |
0.3620 |
0.7770 |
600.00 |
0.4390 |
0.8270 |
600.00 |
0.4980 |
0.8540 |
600.00 |
0.5390 |
0.9160 |
600.00 |
0.7080 |
0.9760 |
600.00 |
0.8930 |
0.9840 |
600.00 |
0.9330 |
0.9910 |
600.00 |
0.9640 |
1.0000 |
600.00 |
1.0000 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
781.3 |
0.0385 |
786.8 |
0.0995 |
794.8 |
0.1656 |
803.2 |
0.2024 |
807.5 |
0.3568 |
824.3 |
0.3010 |
818.5 |
0.3489 |
823.5 |
0.4058 |
829.2 |
0.4596 |
834.3 |
0.5485 |
842.3 |
0.6017 |
846.8 |
0.6534 |
851.0 |
0.7058 |
855.2 |
0.7462 |
858.3 |
0.8033 |
862.6 |
0.8568 |
866.5 |
0.9003 |
869.6 |
0.9484 |
872.9 |
1.0000 |
876.5 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
781.3 |
0.0385 |
786.8 |
0.0995 |
794.8 |
0.1656 |
803.2 |
0.2024 |
807.5 |
0.3568 |
824.3 |
0.3010 |
818.5 |
0.3489 |
823.5 |
0.4058 |
829.2 |
0.4596 |
834.3 |
0.5485 |
842.3 |
0.6017 |
846.8 |
0.6534 |
851.0 |
0.7058 |
855.2 |
0.7462 |
858.3 |
0.8033 |
862.6 |
0.8568 |
866.5 |
0.9003 |
869.6 |
0.9484 |
872.9 |
1.0000 |
876.5 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.9102 |
356.67 |
0.7426 |
359.90 |
0.6093 |
362.92 |
0.4600 |
366.67 |
0.3704 |
369.95 |
0.2893 |
373.58 |
0.2151 |
377.27 |
0.1834 |
379.26 |
0.1293 |
383.45 |
0.1004 |
385.99 |
0.0795 |
387.96 |
0.0381 |
393.30 |
0.0204 |
395.67 |
0.0000 |
399.26 |
1.0000 |
355.27 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
150.00 |
365.78 |
0.0140 |
150.00 |
366.03 |
0.0200 |
150.00 |
366.30 |
0.0500 |
150.00 |
366.90 |
0.0870 |
150.00 |
367.59 |
0.1120 |
150.00 |
368.26 |
0.1370 |
150.00 |
368.99 |
0.1700 |
150.00 |
369.39 |
0.2000 |
150.00 |
369.94 |
0.2270 |
150.00 |
370.42 |
0.2530 |
150.00 |
370.87 |
0.2850 |
150.00 |
371.48 |
0.3100 |
150.00 |
372.05 |
0.3380 |
150.00 |
372.60 |
0.3660 |
150.00 |
373.02 |
0.3980 |
150.00 |
373.55 |
0.4310 |
150.00 |
374.05 |
0.4590 |
150.00 |
374.79 |
0.4950 |
150.00 |
375.85 |
0.5330 |
150.00 |
376.78 |
0.5500 |
150.00 |
377.94 |
0.5740 |
150.00 |
378.34 |
0.5950 |
150.00 |
379.48 |
0.6830 |
150.00 |
382.83 |
0.7070 |
150.00 |
384.24 |
0.7860 |
150.00 |
387.83 |
0.8580 |
150.00 |
392.22 |
0.9160 |
150.00 |
399.44 |
0.9510 |
150.00 |
403.89 |
0.9730 |
150.00 |
407.86 |
0.9810 |
150.00 |
409.45 |
1.0000 |
150.00 |
413.30 |
0.0000 |
600.00 |
409.88 |
0.0150 |
600.00 |
410.31 |
0.0400 |
600.00 |
410.79 |
0.0690 |
600.00 |
411.93 |
0.1010 |
600.00 |
413.32 |
0.1510 |
600.00 |
414.77 |
0.1750 |
600.00 |
415.61 |
0.2010 |
600.00 |
416.38 |
0.2360 |
600.00 |
417.35 |
0.2550 |
600.00 |
418.58 |
0.2760 |
600.00 |
419.03 |
0.3080 |
600.00 |
420.23 |
0.3260 |
600.00 |
420.78 |
0.3590 |
600.00 |
422.05 |
0.3790 |
600.00 |
423.12 |
0.4050 |
600.00 |
423.93 |
0.4880 |
600.00 |
427.31 |
0.5200 |
600.00 |
429.04 |
0.5770 |
600.00 |
432.02 |
0.6650 |
600.00 |
436.86 |
0.7170 |
600.00 |
439.62 |
0.7770 |
600.00 |
445.51 |
0.8270 |
600.00 |
449.36 |
0.8540 |
600.00 |
451.89 |
0.9160 |
600.00 |
460.24 |
0.9760 |
600.00 |
468.77 |
0.9840 |
600.00 |
471.24 |
0.9910 |
600.00 |
472.76 |
1.0000 |
600.00 |
474.55 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.9102 |
356.67 |
0.7426 |
359.90 |
0.6093 |
362.92 |
0.4600 |
366.67 |
0.3704 |
369.95 |
0.2893 |
373.58 |
0.2151 |
377.27 |
0.1834 |
379.26 |
0.1293 |
383.45 |
0.1004 |
385.99 |
0.0795 |
387.96 |
0.0381 |
393.30 |
0.0204 |
395.67 |
0.0000 |
399.26 |
1.0000 |
355.27 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
150.00 |
365.78 |
0.0140 |
150.00 |
366.03 |
0.0200 |
150.00 |
366.30 |
0.0500 |
150.00 |
366.90 |
0.0870 |
150.00 |
367.59 |
0.1120 |
150.00 |
368.26 |
0.1370 |
150.00 |
368.99 |
0.1700 |
150.00 |
369.39 |
0.2000 |
150.00 |
369.94 |
0.2270 |
150.00 |
370.42 |
0.2530 |
150.00 |
370.87 |
0.2850 |
150.00 |
371.48 |
0.3100 |
150.00 |
372.05 |
0.3380 |
150.00 |
372.60 |
0.3660 |
150.00 |
373.02 |
0.3980 |
150.00 |
373.55 |
0.4310 |
150.00 |
374.05 |
0.4590 |
150.00 |
374.79 |
0.4950 |
150.00 |
375.85 |
0.5330 |
150.00 |
376.78 |
0.5500 |
150.00 |
377.94 |
0.5740 |
150.00 |
378.34 |
0.5950 |
150.00 |
379.48 |
0.6830 |
150.00 |
382.83 |
0.7070 |
150.00 |
384.24 |
0.7860 |
150.00 |
387.83 |
0.8580 |
150.00 |
392.22 |
0.9160 |
150.00 |
399.44 |
0.9510 |
150.00 |
403.89 |
0.9730 |
150.00 |
407.86 |
0.9810 |
150.00 |
409.45 |
1.0000 |
150.00 |
413.30 |
0.0000 |
600.00 |
409.88 |
0.0150 |
600.00 |
410.31 |
0.0400 |
600.00 |
410.79 |
0.0690 |
600.00 |
411.93 |
0.1010 |
600.00 |
413.32 |
0.1510 |
600.00 |
414.77 |
0.1750 |
600.00 |
415.61 |
0.2010 |
600.00 |
416.38 |
0.2360 |
600.00 |
417.35 |
0.2550 |
600.00 |
418.58 |
0.2760 |
600.00 |
419.03 |
0.3080 |
600.00 |
420.23 |
0.3260 |
600.00 |
420.78 |
0.3590 |
600.00 |
422.05 |
0.3790 |
600.00 |
423.12 |
0.4050 |
600.00 |
423.93 |
0.4880 |
600.00 |
427.31 |
0.5200 |
600.00 |
429.04 |
0.5770 |
600.00 |
432.02 |
0.6650 |
600.00 |
436.86 |
0.7170 |
600.00 |
439.62 |
0.7770 |
600.00 |
445.51 |
0.8270 |
600.00 |
449.36 |
0.8540 |
600.00 |
451.89 |
0.9160 |
600.00 |
460.24 |
0.9760 |
600.00 |
468.77 |
0.9840 |
600.00 |
471.24 |
0.9910 |
600.00 |
472.76 |
1.0000 |
600.00 |
474.55 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Isopropyl Alcohol (1) - Liquid |
y1[mol/mol] of Isopropyl Alcohol (1) - Vapour |
398.3 |
0.0050 |
0.0420 |
396.82 |
0.0120 |
0.0990 |
375.9 |
0.2150 |
0.5930 |
372.33 |
0.2750 |
0.6580 |
366.71 |
0.4150 |
0.7620 |
364.54 |
0.4880 |
0.8090 |
362.19 |
0.5850 |
0.8400 |
360.8 |
0.6520 |
0.8650 |
359.39 |
0.7270 |
0.8940 |
358.3 |
0.7960 |
0.9170 |
356.82 |
0.8930 |
0.9520 |
356.38 |
0.9220 |
0.9650 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
46.66 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Isopropyl Alcohol (1) - Liquid |
y1[mol/mol] of Isopropyl Alcohol (1) - Vapour |
373.58 |
0.0040 |
0.0290 |
369.29 |
0.0290 |
0.1690 |
364.93 |
0.0670 |
0.3140 |
361.31 |
0.1010 |
0.4130 |
356.31 |
0.1630 |
0.5390 |
353.98 |
0.2010 |
0.5920 |
350.34 |
0.2720 |
0.6740 |
346.45 |
0.3860 |
0.7500 |
344.44 |
0.4740 |
0.7930 |
342.61 |
0.5760 |
0.8320 |
341.35 |
0.6520 |
0.8600 |
340.42 |
0.7250 |
0.8850 |
339.51 |
0.7990 |
0.9110 |
338.43 |
0.8920 |
0.9480 |
338.12 |
0.9230 |
0.9610 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.32 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Isopropyl Alcohol (1) - Liquid |
y1[mol/mol] of Isopropyl Alcohol (1) - Vapour |
399.26 |
0.0000 |
0.0000 |
393.15 |
0.0345 |
0.1920 |
389.35 |
0.0619 |
0.3015 |
387.39 |
0.0766 |
0.3488 |
384.89 |
0.0987 |
0.4096 |
382.93 |
0.1153 |
0.4465 |
380.62 |
0.1398 |
0.4946 |
379.32 |
0.1545 |
0.5209 |
378.75 |
0.1634 |
0.5358 |
377.55 |
0.1792 |
0.5588 |
375.53 |
0.2102 |
0.6011 |
373.45 |
0.2426 |
0.6395 |
371.29 |
0.2868 |
0.6782 |
369.4 |
0.3280 |
0.7147 |
367.5 |
0.3742 |
0.7456 |
365.81 |
0.4219 |
0.7769 |
364.3 |
0.4728 |
0.8016 |
362.54 |
0.5430 |
0.8304 |
361.31 |
0.5968 |
0.8506 |
360.32 |
0.6475 |
0.8697 |
359.1 |
0.7219 |
0.8921 |
358.13 |
0.7704 |
0.9095 |
357.32 |
0.8172 |
0.9290 |
356.82 |
0.8671 |
0.9470 |
356.15 |
0.9134 |
0.9655 |
355.41 |
0.9610 |
0.9830 |
355.4 |
1.0000 |
1.0000 |
Sources