Datasets
-
Mole fraction (14)
-
n0 - Refractive index (Na D-line) (4)
-
ρl - Mass density, kg/m3 (4)
-
Tc - Critical temperature, K (2)
-
Vapor Liquid Equilibrium at Constant Pressure (2)
Mole fraction
[ref]
Operational conditions:
- Temperature, K = 308.15 (Liquid mixture 1)
- Pressure, kPa = 101 (Liquid mixture 1)
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
0.9230 |
0.0000 |
0.0010 |
0.0000 |
0.3120 |
0.2820 |
0.0080 |
0.1420 |
0.2600 |
0.2900 |
0.0120 |
0.1610 |
0.2030 |
0.2910 |
0.0200 |
0.1810 |
0.1390 |
0.2750 |
0.0400 |
0.2060 |
0.8570 |
0.0270 |
0.0010 |
0.0090 |
0.7980 |
0.0610 |
0.0010 |
0.0200 |
0.7200 |
0.1040 |
0.0020 |
0.0360 |
0.6440 |
0.1500 |
0.0010 |
0.0530 |
0.5680 |
0.1880 |
0.0020 |
0.0690 |
0.4920 |
0.2240 |
0.0030 |
0.0890 |
0.4210 |
0.2480 |
0.0040 |
0.1050 |
0.3570 |
0.2700 |
0.0060 |
0.1260 |
Mole fraction in LLG critical state of Acetic acid (2)
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Temperature, K - Liquid |
Mole fraction in LLG critical state of Acetic acid (2) - Liquid |
0.1330 |
308.15 |
0.2600 |
Mole fraction of Water (3)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
293.20 |
0.9296 |
0.0704 |
293.20 |
0.6905 |
0.1756 |
293.20 |
0.5335 |
0.2579 |
293.20 |
0.3526 |
0.3721 |
293.20 |
0.2468 |
0.4636 |
293.20 |
0.1848 |
0.5307 |
293.20 |
0.1424 |
0.5857 |
293.20 |
0.0791 |
0.6776 |
293.20 |
0.0502 |
0.7252 |
293.20 |
0.0222 |
0.7888 |
293.20 |
0.0107 |
0.8385 |
293.20 |
0.0049 |
0.8906 |
293.20 |
0.0048 |
0.9360 |
293.20 |
0.0015 |
0.9673 |
293.20 |
0.0012 |
0.9988 |
313.20 |
0.9145 |
0.0855 |
313.20 |
0.6346 |
0.2227 |
313.20 |
0.4658 |
0.3082 |
313.20 |
0.3449 |
0.3917 |
313.20 |
0.2453 |
0.4776 |
313.20 |
0.1729 |
0.5571 |
313.20 |
0.1095 |
0.6420 |
313.20 |
0.0548 |
0.7261 |
313.20 |
0.0219 |
0.7979 |
313.20 |
0.0120 |
0.8364 |
313.20 |
0.0060 |
0.8829 |
313.20 |
0.0034 |
0.9192 |
313.20 |
0.0024 |
0.9417 |
313.20 |
0.0016 |
0.9678 |
313.20 |
0.0012 |
0.9988 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
293.20 |
0.9670 |
0.0327 |
0.0680 |
0.1189 |
293.20 |
0.9380 |
0.0604 |
0.1259 |
0.1686 |
293.20 |
0.9086 |
0.0873 |
0.1846 |
0.2301 |
293.20 |
0.8787 |
0.1134 |
0.2266 |
0.2866 |
293.20 |
0.8480 |
0.1385 |
0.2648 |
0.3601 |
293.20 |
0.8066 |
0.1700 |
0.2879 |
0.4475 |
313.20 |
0.9684 |
0.0312 |
0.0695 |
0.1414 |
313.20 |
0.9362 |
0.0625 |
0.1260 |
0.1935 |
313.20 |
0.9065 |
0.0897 |
0.1769 |
0.2503 |
313.20 |
0.8769 |
0.1153 |
0.2198 |
0.3119 |
313.20 |
0.8424 |
0.1431 |
0.2553 |
0.3861 |
Mole fraction of Acetic acid (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 318.15 (Liquid mixture 1)
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
0.7820 |
0.0950 |
0.7460 |
0.1120 |
0.6980 |
0.1300 |
0.6580 |
0.1540 |
0.5740 |
0.1850 |
0.5180 |
0.2060 |
0.4710 |
0.2280 |
0.3530 |
0.2690 |
0.2950 |
0.2730 |
0.2640 |
0.2760 |
0.2410 |
0.2760 |
0.2150 |
0.2740 |
0.1930 |
0.2700 |
0.1570 |
0.2600 |
0.1410 |
0.2550 |
0.1180 |
0.2450 |
0.1000 |
0.2370 |
0.0740 |
0.2260 |
0.0590 |
0.2170 |
Mole fraction
[ref]
Operational conditions:
- Temperature, K = 318.15 (Liquid mixture 1)
- Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed |
Measured |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
0.0170 |
0.0050 |
0.0310 |
0.8710 |
0.0330 |
0.0050 |
0.0770 |
0.8010 |
0.0490 |
0.0060 |
0.1210 |
0.7420 |
0.0700 |
0.0050 |
0.1610 |
0.6500 |
0.0960 |
0.0090 |
0.2140 |
0.5080 |
0.1190 |
0.0120 |
0.2520 |
0.4220 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
304.15 |
0.1020 |
0.0000 |
0.9995 |
0.0000 |
304.15 |
0.1529 |
0.0396 |
0.9850 |
0.0140 |
304.15 |
0.1737 |
0.0808 |
0.9709 |
0.0277 |
304.15 |
0.2099 |
0.1215 |
0.9579 |
0.0403 |
304.15 |
0.2434 |
0.1563 |
0.9419 |
0.0558 |
304.15 |
0.2832 |
0.1929 |
0.9264 |
0.0704 |
304.15 |
0.3261 |
0.2166 |
0.9088 |
0.0869 |
304.15 |
0.3839 |
0.2396 |
0.8910 |
0.1028 |
304.15 |
0.4050 |
0.2532 |
0.8796 |
0.1127 |
332.15 |
0.1316 |
0.0000 |
0.9992 |
0.0000 |
332.15 |
0.1774 |
0.0435 |
0.9850 |
0.0137 |
332.15 |
0.2086 |
0.0800 |
0.9716 |
0.0271 |
332.15 |
0.2327 |
0.1176 |
0.9557 |
0.0424 |
332.15 |
0.3031 |
0.1854 |
0.9386 |
0.0575 |
332.15 |
0.3466 |
0.2087 |
0.9031 |
0.0910 |
332.15 |
0.3813 |
0.2427 |
0.8874 |
0.1044 |
332.15 |
0.4000 |
0.2502 |
0.8629 |
0.1267 |
366.15 |
0.5061 |
0.2617 |
0.8263 |
0.1557 |
366.15 |
0.1732 |
0.0386 |
0.9850 |
0.0136 |
366.15 |
0.1573 |
0.0000 |
0.9991 |
0.0000 |
366.15 |
0.2024 |
0.0761 |
0.9710 |
0.0268 |
366.15 |
0.2182 |
0.1134 |
0.9526 |
0.0436 |
366.15 |
0.3052 |
0.1788 |
0.9208 |
0.0744 |
366.15 |
0.3309 |
0.2098 |
0.8958 |
0.0982 |
366.15 |
0.3950 |
0.2251 |
0.8802 |
0.1111 |
Mole fraction
[ref]
Operational conditions:
- Temperature, K = 308.15 (Liquid mixture 1)
- Pressure, kPa = 101 (Liquid mixture 1)
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
0.9230 |
0.0000 |
0.0010 |
0.0000 |
0.3120 |
0.2820 |
0.0080 |
0.1420 |
0.2600 |
0.2900 |
0.0120 |
0.1610 |
0.2030 |
0.2910 |
0.0200 |
0.1810 |
0.1390 |
0.2750 |
0.0400 |
0.2060 |
0.8570 |
0.0270 |
0.0010 |
0.0090 |
0.7980 |
0.0610 |
0.0010 |
0.0200 |
0.7200 |
0.1040 |
0.0020 |
0.0360 |
0.6440 |
0.1500 |
0.0010 |
0.0530 |
0.5680 |
0.1880 |
0.0020 |
0.0690 |
0.4920 |
0.2240 |
0.0030 |
0.0890 |
0.4210 |
0.2480 |
0.0040 |
0.1050 |
0.3570 |
0.2700 |
0.0060 |
0.1260 |
Mole fraction in LLG critical state of Acetic acid (2)
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Temperature, K - Liquid |
Mole fraction in LLG critical state of Acetic acid (2) - Liquid |
0.1330 |
308.15 |
0.2600 |
Mole fraction of Water (3)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
293.20 |
0.9296 |
0.0704 |
293.20 |
0.6905 |
0.1756 |
293.20 |
0.5335 |
0.2579 |
293.20 |
0.3526 |
0.3721 |
293.20 |
0.2468 |
0.4636 |
293.20 |
0.1848 |
0.5307 |
293.20 |
0.1424 |
0.5857 |
293.20 |
0.0791 |
0.6776 |
293.20 |
0.0502 |
0.7252 |
293.20 |
0.0222 |
0.7888 |
293.20 |
0.0107 |
0.8385 |
293.20 |
0.0049 |
0.8906 |
293.20 |
0.0048 |
0.9360 |
293.20 |
0.0015 |
0.9673 |
293.20 |
0.0012 |
0.9988 |
313.20 |
0.9145 |
0.0855 |
313.20 |
0.6346 |
0.2227 |
313.20 |
0.4658 |
0.3082 |
313.20 |
0.3449 |
0.3917 |
313.20 |
0.2453 |
0.4776 |
313.20 |
0.1729 |
0.5571 |
313.20 |
0.1095 |
0.6420 |
313.20 |
0.0548 |
0.7261 |
313.20 |
0.0219 |
0.7979 |
313.20 |
0.0120 |
0.8364 |
313.20 |
0.0060 |
0.8829 |
313.20 |
0.0034 |
0.9192 |
313.20 |
0.0024 |
0.9417 |
313.20 |
0.0016 |
0.9678 |
313.20 |
0.0012 |
0.9988 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 1 |
293.20 |
0.9670 |
0.0327 |
0.0680 |
0.1189 |
293.20 |
0.9380 |
0.0604 |
0.1259 |
0.1686 |
293.20 |
0.9086 |
0.0873 |
0.1846 |
0.2301 |
293.20 |
0.8787 |
0.1134 |
0.2266 |
0.2866 |
293.20 |
0.8480 |
0.1385 |
0.2648 |
0.3601 |
293.20 |
0.8066 |
0.1700 |
0.2879 |
0.4475 |
313.20 |
0.9684 |
0.0312 |
0.0695 |
0.1414 |
313.20 |
0.9362 |
0.0625 |
0.1260 |
0.1935 |
313.20 |
0.9065 |
0.0897 |
0.1769 |
0.2503 |
313.20 |
0.8769 |
0.1153 |
0.2198 |
0.3119 |
313.20 |
0.8424 |
0.1431 |
0.2553 |
0.3861 |
Mole fraction of Acetic acid (2)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 1)
- Temperature, K = 318.15 (Liquid mixture 1)
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
0.7820 |
0.0950 |
0.7460 |
0.1120 |
0.6980 |
0.1300 |
0.6580 |
0.1540 |
0.5740 |
0.1850 |
0.5180 |
0.2060 |
0.4710 |
0.2280 |
0.3530 |
0.2690 |
0.2950 |
0.2730 |
0.2640 |
0.2760 |
0.2410 |
0.2760 |
0.2150 |
0.2740 |
0.1930 |
0.2700 |
0.1570 |
0.2600 |
0.1410 |
0.2550 |
0.1180 |
0.2450 |
0.1000 |
0.2370 |
0.0740 |
0.2260 |
0.0590 |
0.2170 |
Mole fraction
[ref]
Operational conditions:
- Temperature, K = 318.15 (Liquid mixture 1)
- Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed |
Measured |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
Mole fraction of Acetic acid, butyl ester (1) - Liquid mixture 1 |
0.0170 |
0.0050 |
0.0310 |
0.8710 |
0.0330 |
0.0050 |
0.0770 |
0.8010 |
0.0490 |
0.0060 |
0.1210 |
0.7420 |
0.0700 |
0.0050 |
0.1610 |
0.6500 |
0.0960 |
0.0090 |
0.2140 |
0.5080 |
0.1190 |
0.0120 |
0.2520 |
0.4220 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mole fraction of Water (3) - Liquid mixture 1 |
Mole fraction of Acetic acid (2) - Liquid mixture 1 |
Mole fraction of Water (3) - Liquid mixture 2 |
Mole fraction of Acetic acid (2) - Liquid mixture 2 |
304.15 |
0.1020 |
0.0000 |
0.9995 |
0.0000 |
304.15 |
0.1529 |
0.0396 |
0.9850 |
0.0140 |
304.15 |
0.1737 |
0.0808 |
0.9709 |
0.0277 |
304.15 |
0.2099 |
0.1215 |
0.9579 |
0.0403 |
304.15 |
0.2434 |
0.1563 |
0.9419 |
0.0558 |
304.15 |
0.2832 |
0.1929 |
0.9264 |
0.0704 |
304.15 |
0.3261 |
0.2166 |
0.9088 |
0.0869 |
304.15 |
0.3839 |
0.2396 |
0.8910 |
0.1028 |
304.15 |
0.4050 |
0.2532 |
0.8796 |
0.1127 |
332.15 |
0.1316 |
0.0000 |
0.9992 |
0.0000 |
332.15 |
0.1774 |
0.0435 |
0.9850 |
0.0137 |
332.15 |
0.2086 |
0.0800 |
0.9716 |
0.0271 |
332.15 |
0.2327 |
0.1176 |
0.9557 |
0.0424 |
332.15 |
0.3031 |
0.1854 |
0.9386 |
0.0575 |
332.15 |
0.3466 |
0.2087 |
0.9031 |
0.0910 |
332.15 |
0.3813 |
0.2427 |
0.8874 |
0.1044 |
332.15 |
0.4000 |
0.2502 |
0.8629 |
0.1267 |
366.15 |
0.5061 |
0.2617 |
0.8263 |
0.1557 |
366.15 |
0.1732 |
0.0386 |
0.9850 |
0.0136 |
366.15 |
0.1573 |
0.0000 |
0.9991 |
0.0000 |
366.15 |
0.2024 |
0.0761 |
0.9710 |
0.0268 |
366.15 |
0.2182 |
0.1134 |
0.9526 |
0.0436 |
366.15 |
0.3052 |
0.1788 |
0.9208 |
0.0744 |
366.15 |
0.3309 |
0.2098 |
0.8958 |
0.0982 |
366.15 |
0.3950 |
0.2251 |
0.8802 |
0.1111 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Refractive index (Na D-line) - Liquid |
293.20 |
0.0704 |
0.9296 |
1.3939 |
293.20 |
0.1756 |
0.6905 |
1.3922 |
293.20 |
0.2579 |
0.5335 |
1.3905 |
293.20 |
0.3721 |
0.3526 |
1.3875 |
293.20 |
0.4636 |
0.2468 |
1.3847 |
293.20 |
0.5307 |
0.1848 |
1.3825 |
293.20 |
0.5857 |
0.1424 |
1.3801 |
293.20 |
0.6776 |
0.0791 |
1.3751 |
293.20 |
0.7252 |
0.0502 |
1.3716 |
293.20 |
0.7888 |
0.0222 |
1.3661 |
293.20 |
0.8385 |
0.0107 |
1.3611 |
293.20 |
0.8906 |
0.0049 |
1.3542 |
293.20 |
0.9360 |
0.0048 |
1.3468 |
293.20 |
0.9673 |
0.0015 |
1.341 |
293.20 |
0.9988 |
0.0012 |
1.3337 |
313.20 |
0.0855 |
0.9145 |
1.3843 |
313.20 |
0.2227 |
0.6346 |
1.3824 |
313.20 |
0.3082 |
0.4658 |
1.3803 |
313.20 |
0.3917 |
0.3449 |
1.3786 |
313.20 |
0.4776 |
0.2453 |
1.3762 |
313.20 |
0.5571 |
0.1729 |
1.3769 |
313.20 |
0.6420 |
0.1095 |
1.3676 |
313.20 |
0.7261 |
0.0548 |
1.3653 |
313.20 |
0.7979 |
0.0219 |
1.3592 |
313.20 |
0.8364 |
0.0120 |
1.3553 |
313.20 |
0.8829 |
0.0060 |
1.3499 |
313.20 |
0.9192 |
0.0034 |
1.3452 |
313.20 |
0.9417 |
0.0024 |
1.3417 |
313.20 |
0.9678 |
0.0016 |
1.3372 |
313.20 |
0.9988 |
0.0012 |
1.3307 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid (2) - Liquid |
Refractive index (Na D-line) - Liquid |
293.20 |
0.1189 |
0.0680 |
1.3932 |
293.20 |
0.1686 |
0.1259 |
1.3922 |
293.20 |
0.2301 |
0.1846 |
1.3909 |
293.20 |
0.2866 |
0.2266 |
1.3897 |
293.20 |
0.3601 |
0.2648 |
1.3879 |
293.20 |
0.4475 |
0.2879 |
1.3854 |
293.20 |
0.9670 |
0.0327 |
1.3406 |
293.20 |
0.9380 |
0.0604 |
1.3458 |
293.20 |
0.9086 |
0.0873 |
1.3508 |
293.20 |
0.8787 |
0.1134 |
1.3554 |
293.20 |
0.8480 |
0.1385 |
1.3598 |
293.20 |
0.8066 |
0.1700 |
1.3648 |
313.20 |
0.1414 |
0.0695 |
1.3836 |
313.20 |
0.1935 |
0.1260 |
1.3828 |
313.20 |
0.2503 |
0.1769 |
1.3817 |
313.20 |
0.3119 |
0.2198 |
1.3806 |
313.20 |
0.3861 |
0.2553 |
1.379 |
313.20 |
0.9684 |
0.0312 |
1.3366 |
313.20 |
0.9362 |
0.0625 |
1.3416 |
313.20 |
0.9065 |
0.0897 |
1.346 |
313.20 |
0.8769 |
0.1153 |
1.3502 |
313.20 |
0.8424 |
0.1431 |
1.3547 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Refractive index (Na D-line) - Liquid |
293.20 |
0.0704 |
0.9296 |
1.3939 |
293.20 |
0.1756 |
0.6905 |
1.3922 |
293.20 |
0.2579 |
0.5335 |
1.3905 |
293.20 |
0.3721 |
0.3526 |
1.3875 |
293.20 |
0.4636 |
0.2468 |
1.3847 |
293.20 |
0.5307 |
0.1848 |
1.3825 |
293.20 |
0.5857 |
0.1424 |
1.3801 |
293.20 |
0.6776 |
0.0791 |
1.3751 |
293.20 |
0.7252 |
0.0502 |
1.3716 |
293.20 |
0.7888 |
0.0222 |
1.3661 |
293.20 |
0.8385 |
0.0107 |
1.3611 |
293.20 |
0.8906 |
0.0049 |
1.3542 |
293.20 |
0.9360 |
0.0048 |
1.3468 |
293.20 |
0.9673 |
0.0015 |
1.341 |
293.20 |
0.9988 |
0.0012 |
1.3337 |
313.20 |
0.0855 |
0.9145 |
1.3843 |
313.20 |
0.2227 |
0.6346 |
1.3824 |
313.20 |
0.3082 |
0.4658 |
1.3803 |
313.20 |
0.3917 |
0.3449 |
1.3786 |
313.20 |
0.4776 |
0.2453 |
1.3762 |
313.20 |
0.5571 |
0.1729 |
1.3769 |
313.20 |
0.6420 |
0.1095 |
1.3676 |
313.20 |
0.7261 |
0.0548 |
1.3653 |
313.20 |
0.7979 |
0.0219 |
1.3592 |
313.20 |
0.8364 |
0.0120 |
1.3553 |
313.20 |
0.8829 |
0.0060 |
1.3499 |
313.20 |
0.9192 |
0.0034 |
1.3452 |
313.20 |
0.9417 |
0.0024 |
1.3417 |
313.20 |
0.9678 |
0.0016 |
1.3372 |
313.20 |
0.9988 |
0.0012 |
1.3307 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid (2) - Liquid |
Refractive index (Na D-line) - Liquid |
293.20 |
0.1189 |
0.0680 |
1.3932 |
293.20 |
0.1686 |
0.1259 |
1.3922 |
293.20 |
0.2301 |
0.1846 |
1.3909 |
293.20 |
0.2866 |
0.2266 |
1.3897 |
293.20 |
0.3601 |
0.2648 |
1.3879 |
293.20 |
0.4475 |
0.2879 |
1.3854 |
293.20 |
0.9670 |
0.0327 |
1.3406 |
293.20 |
0.9380 |
0.0604 |
1.3458 |
293.20 |
0.9086 |
0.0873 |
1.3508 |
293.20 |
0.8787 |
0.1134 |
1.3554 |
293.20 |
0.8480 |
0.1385 |
1.3598 |
293.20 |
0.8066 |
0.1700 |
1.3648 |
313.20 |
0.1414 |
0.0695 |
1.3836 |
313.20 |
0.1935 |
0.1260 |
1.3828 |
313.20 |
0.2503 |
0.1769 |
1.3817 |
313.20 |
0.3119 |
0.2198 |
1.3806 |
313.20 |
0.3861 |
0.2553 |
1.379 |
313.20 |
0.9684 |
0.0312 |
1.3366 |
313.20 |
0.9362 |
0.0625 |
1.3416 |
313.20 |
0.9065 |
0.0897 |
1.346 |
313.20 |
0.8769 |
0.1153 |
1.3502 |
313.20 |
0.8424 |
0.1431 |
1.3547 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.20 |
0.0704 |
0.9296 |
882.76 |
293.20 |
0.1756 |
0.6905 |
900.332 |
293.20 |
0.2579 |
0.5335 |
915.524 |
293.20 |
0.3721 |
0.3526 |
940.057 |
293.20 |
0.4636 |
0.2468 |
959.781 |
293.20 |
0.5307 |
0.1848 |
974.031 |
293.20 |
0.5857 |
0.1424 |
985.602 |
293.20 |
0.6776 |
0.0791 |
1007.941 |
293.20 |
0.7252 |
0.0502 |
1020.682 |
293.20 |
0.7888 |
0.0222 |
1034.909 |
293.20 |
0.8385 |
0.0107 |
1037.792 |
293.20 |
0.8906 |
0.0049 |
1032.799 |
293.20 |
0.9360 |
0.0048 |
1020.951 |
293.20 |
0.9673 |
0.0015 |
1011.642 |
293.20 |
0.9988 |
0.0012 |
998.132 |
313.20 |
0.0855 |
0.9145 |
862.224 |
313.20 |
0.2227 |
0.6346 |
882.496 |
313.20 |
0.3082 |
0.4658 |
902.04 |
313.20 |
0.3917 |
0.3449 |
917.886 |
313.20 |
0.4776 |
0.2453 |
938.395 |
313.20 |
0.5571 |
0.1729 |
954.613 |
313.20 |
0.6420 |
0.1095 |
972.431 |
313.20 |
0.7261 |
0.0548 |
1004.372 |
313.20 |
0.7979 |
0.0219 |
1018.167 |
313.20 |
0.8364 |
0.0120 |
1021.961 |
313.20 |
0.8829 |
0.0060 |
1020.388 |
313.20 |
0.9192 |
0.0034 |
1015.299 |
313.20 |
0.9417 |
0.0024 |
1010.408 |
313.20 |
0.9678 |
0.0016 |
1003.113 |
313.20 |
0.9988 |
0.0012 |
992.026 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.20 |
0.1189 |
0.0680 |
890.768 |
293.20 |
0.1686 |
0.1259 |
899.53 |
293.20 |
0.2301 |
0.1846 |
910.833 |
293.20 |
0.2866 |
0.2266 |
921.883 |
293.20 |
0.3601 |
0.2648 |
936.765 |
293.20 |
0.4475 |
0.2879 |
955.524 |
293.20 |
0.9670 |
0.0327 |
1010.719 |
293.20 |
0.9380 |
0.0604 |
1020.131 |
293.20 |
0.9086 |
0.0873 |
1028.427 |
293.20 |
0.8787 |
0.1134 |
1033.817 |
293.20 |
0.8480 |
0.1385 |
1037.365 |
293.20 |
0.8066 |
0.1700 |
1036.027 |
313.20 |
0.1414 |
0.0695 |
870.595 |
313.20 |
0.1935 |
0.1260 |
879.87 |
313.20 |
0.2503 |
0.1769 |
890.018 |
313.20 |
0.3119 |
0.2198 |
902.003 |
313.20 |
0.3861 |
0.2553 |
917.061 |
313.20 |
0.9684 |
0.0312 |
1002.259 |
313.20 |
0.9362 |
0.0625 |
1010.186 |
313.20 |
0.9065 |
0.0897 |
1015.976 |
313.20 |
0.8769 |
0.1153 |
1020.245 |
313.20 |
0.8424 |
0.1431 |
1021.524 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.20 |
0.0704 |
0.9296 |
882.76 |
293.20 |
0.1756 |
0.6905 |
900.332 |
293.20 |
0.2579 |
0.5335 |
915.524 |
293.20 |
0.3721 |
0.3526 |
940.057 |
293.20 |
0.4636 |
0.2468 |
959.781 |
293.20 |
0.5307 |
0.1848 |
974.031 |
293.20 |
0.5857 |
0.1424 |
985.602 |
293.20 |
0.6776 |
0.0791 |
1007.941 |
293.20 |
0.7252 |
0.0502 |
1020.682 |
293.20 |
0.7888 |
0.0222 |
1034.909 |
293.20 |
0.8385 |
0.0107 |
1037.792 |
293.20 |
0.8906 |
0.0049 |
1032.799 |
293.20 |
0.9360 |
0.0048 |
1020.951 |
293.20 |
0.9673 |
0.0015 |
1011.642 |
293.20 |
0.9988 |
0.0012 |
998.132 |
313.20 |
0.0855 |
0.9145 |
862.224 |
313.20 |
0.2227 |
0.6346 |
882.496 |
313.20 |
0.3082 |
0.4658 |
902.04 |
313.20 |
0.3917 |
0.3449 |
917.886 |
313.20 |
0.4776 |
0.2453 |
938.395 |
313.20 |
0.5571 |
0.1729 |
954.613 |
313.20 |
0.6420 |
0.1095 |
972.431 |
313.20 |
0.7261 |
0.0548 |
1004.372 |
313.20 |
0.7979 |
0.0219 |
1018.167 |
313.20 |
0.8364 |
0.0120 |
1021.961 |
313.20 |
0.8829 |
0.0060 |
1020.388 |
313.20 |
0.9192 |
0.0034 |
1015.299 |
313.20 |
0.9417 |
0.0024 |
1010.408 |
313.20 |
0.9678 |
0.0016 |
1003.113 |
313.20 |
0.9988 |
0.0012 |
992.026 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Water (3) - Liquid |
Mole fraction of Acetic acid (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.20 |
0.1189 |
0.0680 |
890.768 |
293.20 |
0.1686 |
0.1259 |
899.53 |
293.20 |
0.2301 |
0.1846 |
910.833 |
293.20 |
0.2866 |
0.2266 |
921.883 |
293.20 |
0.3601 |
0.2648 |
936.765 |
293.20 |
0.4475 |
0.2879 |
955.524 |
293.20 |
0.9670 |
0.0327 |
1010.719 |
293.20 |
0.9380 |
0.0604 |
1020.131 |
293.20 |
0.9086 |
0.0873 |
1028.427 |
293.20 |
0.8787 |
0.1134 |
1033.817 |
293.20 |
0.8480 |
0.1385 |
1037.365 |
293.20 |
0.8066 |
0.1700 |
1036.027 |
313.20 |
0.1414 |
0.0695 |
870.595 |
313.20 |
0.1935 |
0.1260 |
879.87 |
313.20 |
0.2503 |
0.1769 |
890.018 |
313.20 |
0.3119 |
0.2198 |
902.003 |
313.20 |
0.3861 |
0.2553 |
917.061 |
313.20 |
0.9684 |
0.0312 |
1002.259 |
313.20 |
0.9362 |
0.0625 |
1010.186 |
313.20 |
0.9065 |
0.0897 |
1015.976 |
313.20 |
0.8769 |
0.1153 |
1020.245 |
313.20 |
0.8424 |
0.1431 |
1021.524 |
Critical temperature, K
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid (2) - Liquid |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Critical temperature, K - Liquid |
0.2500 |
0.1050 |
318.15 |
Critical temperature, K
[ref]
Fixed |
Measured |
Mole fraction of Acetic acid (2) - Liquid |
Mole fraction of Acetic acid, butyl ester (1) - Liquid |
Critical temperature, K - Liquid |
0.2500 |
0.1050 |
318.15 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Water (3) - Liquid |
x2[mol/mol] of Acetic acid (2) - Liquid |
y1[mol/mol] of Water (3) - Vapour |
y2[mol/mol] of Acetic acid (2) - Vapour |
371.05 |
0.4466 |
0.3756 |
0.6713 |
0.1369 |
371.65 |
0.2060 |
0.3025 |
0.6842 |
0.0657 |
369.75 |
0.7072 |
0.2357 |
0.7294 |
0.0825 |
369.25 |
0.6302 |
0.2292 |
0.6997 |
0.0769 |
367.25 |
0.5090 |
0.1518 |
0.7011 |
0.0455 |
367.95 |
0.8612 |
0.1222 |
0.7225 |
0.0508 |
368.35 |
0.8800 |
0.1028 |
0.7016 |
0.0607 |
366.85 |
0.8748 |
0.0687 |
0.7006 |
0.0413 |
367.55 |
0.9626 |
0.0360 |
0.7326 |
0.0123 |
365.75 |
0.9580 |
0.0368 |
0.7235 |
0.0089 |
365.45 |
0.8647 |
0.0406 |
0.7066 |
0.0093 |
365.95 |
0.5852 |
0.0976 |
0.7072 |
0.0307 |
367.75 |
0.6952 |
0.2164 |
0.7091 |
0.0709 |
365.75 |
0.8965 |
0.0607 |
0.7132 |
0.0304 |
367.45 |
0.7903 |
0.1721 |
0.7079 |
0.0743 |
375.45 |
0.3755 |
0.5067 |
0.5533 |
0.2682 |
380.55 |
0.1999 |
0.6850 |
0.4403 |
0.4636 |
376.65 |
0.4373 |
0.5250 |
0.6253 |
0.3071 |
364.85 |
0.3924 |
0.1236 |
0.6950 |
0.0218 |
381.35 |
0.2512 |
0.7143 |
0.3774 |
0.5686 |
378.15 |
0.4018 |
0.5709 |
0.5740 |
0.3810 |
375.65 |
0.5524 |
0.4270 |
0.6585 |
0.2575 |
375.55 |
0.5724 |
0.4078 |
0.6804 |
0.2577 |
375.05 |
0.6271 |
0.3556 |
0.7170 |
0.2256 |
373.95 |
0.6683 |
0.3164 |
0.7336 |
0.1906 |
373.75 |
0.7021 |
0.2842 |
0.7525 |
0.1702 |
383.15 |
0.1521 |
0.7651 |
0.3761 |
0.5675 |
379.95 |
0.2645 |
0.6640 |
0.4230 |
0.4865 |
378.05 |
0.3501 |
0.5863 |
0.5187 |
0.3952 |
376.75 |
0.4180 |
0.5254 |
0.5554 |
0.3494 |
375.65 |
0.4715 |
0.4769 |
0.5911 |
0.3005 |
374.95 |
0.5177 |
0.4354 |
0.6540 |
0.2575 |
374.25 |
0.5558 |
0.4007 |
0.6712 |
0.2289 |
373.85 |
0.5883 |
0.3712 |
0.6769 |
0.2175 |
372.45 |
0.6417 |
0.3233 |
0.7102 |
0.1707 |
372.05 |
0.6820 |
0.2869 |
0.7222 |
0.1538 |
382.35 |
0.1615 |
0.7069 |
0.3618 |
0.5224 |
378.95 |
0.2766 |
0.6102 |
0.4548 |
0.4206 |
376.55 |
0.3655 |
0.5350 |
0.5356 |
0.3407 |
375.05 |
0.4337 |
0.4777 |
0.5812 |
0.2919 |
374.05 |
0.4900 |
0.4302 |
0.6358 |
0.2315 |
373.35 |
0.5357 |
0.3915 |
0.6681 |
0.2050 |
372.45 |
0.5731 |
0.3598 |
0.6847 |
0.1789 |
371.95 |
0.6059 |
0.3326 |
0.6904 |
0.1655 |
371.35 |
0.6329 |
0.3096 |
0.7062 |
0.1434 |
372.15 |
0.6570 |
0.2893 |
0.7131 |
0.1393 |
381.05 |
0.1690 |
0.6443 |
0.3316 |
0.4948 |
377.05 |
0.2900 |
0.5506 |
0.4905 |
0.3515 |
374.15 |
0.4505 |
0.4263 |
0.5952 |
0.2426 |
373.15 |
0.5050 |
0.3841 |
0.6276 |
0.2118 |
371.55 |
0.5519 |
0.3475 |
0.6666 |
0.1582 |
370.95 |
0.5954 |
0.3153 |
0.6650 |
0.1470 |
370.25 |
0.6222 |
0.2929 |
0.6956 |
0.1235 |
369.95 |
0.6496 |
0.2717 |
0.6866 |
0.1167 |
369.35 |
0.6720 |
0.2543 |
0.7327 |
0.1026 |
369.05 |
0.6930 |
0.2381 |
0.7037 |
0.1032 |
379.35 |
0.1805 |
0.5715 |
0.4398 |
0.3716 |
375.25 |
0.3072 |
0.4835 |
0.5530 |
0.2611 |
373.05 |
0.3981 |
0.4199 |
0.6189 |
0.1990 |
372.05 |
0.4704 |
0.3693 |
0.6455 |
0.1707 |
370.75 |
0.5258 |
0.3309 |
0.6811 |
0.1271 |
370.15 |
0.5716 |
0.2991 |
0.6898 |
0.1178 |
369.05 |
0.6403 |
0.2509 |
0.6909 |
0.0914 |
368.55 |
0.6896 |
0.2166 |
0.6684 |
0.0819 |
373.35 |
0.3237 |
0.4100 |
0.6136 |
0.1826 |
370.05 |
0.4899 |
0.3092 |
0.6497 |
0.1188 |
367.85 |
0.6593 |
0.2065 |
0.7378 |
0.0660 |
367.35 |
0.7430 |
0.1557 |
0.7053 |
0.0636 |
370.95 |
0.3447 |
0.3263 |
0.6413 |
0.1280 |
367.45 |
0.6125 |
0.1928 |
0.6579 |
0.0572 |
367.05 |
0.7251 |
0.1368 |
0.6944 |
0.0447 |
366.55 |
0.7870 |
0.1060 |
0.6893 |
0.0386 |
368.35 |
0.3658 |
0.2318 |
0.6602 |
0.0674 |
366.75 |
0.5365 |
0.1691 |
0.6455 |
0.0476 |
385.65 |
0.0694 |
0.8336 |
0.2385 |
0.6959 |
383.25 |
0.1064 |
0.7450 |
0.2984 |
0.5901 |
380.65 |
0.1418 |
0.6546 |
0.3284 |
0.5010 |
378.75 |
0.1790 |
0.5595 |
0.4163 |
0.3802 |
375.45 |
0.2213 |
0.4579 |
0.5172 |
0.2478 |
372.15 |
0.2656 |
0.3516 |
0.5901 |
0.1565 |
368.65 |
0.3090 |
0.2409 |
0.6507 |
0.0862 |
386.95 |
0.0340 |
0.9185 |
0.1232 |
0.8400 |
387.45 |
0.0168 |
0.9624 |
0.0619 |
0.9164 |
387.45 |
0.0267 |
0.9515 |
0.0921 |
0.8892 |
384.15 |
0.1073 |
0.8052 |
0.2864 |
0.6497 |
381.05 |
0.1586 |
0.7089 |
0.3436 |
0.5498 |
378.55 |
0.2133 |
0.6097 |
0.4118 |
0.4316 |
374.75 |
0.2684 |
0.5097 |
0.5091 |
0.3006 |
372.25 |
0.3238 |
0.4091 |
0.5845 |
0.1984 |
368.65 |
0.3796 |
0.3079 |
0.6329 |
0.1163 |
387.35 |
0.0267 |
0.9515 |
0.0682 |
0.9087 |
391.85 |
0.0899 |
0.8817 |
0.1459 |
0.8180 |
386.85 |
0.1270 |
0.8287 |
0.1973 |
0.7505 |
378.65 |
0.2687 |
0.6306 |
0.4499 |
0.4480 |
366.45 |
0.5802 |
0.1927 |
0.6771 |
0.0715 |
387.25 |
0.0523 |
0.9295 |
0.0982 |
0.8806 |
385.55 |
0.0808 |
0.8906 |
0.1426 |
0.8252 |
382.15 |
0.1728 |
0.7590 |
0.2901 |
0.6311 |
379.15 |
0.2588 |
0.6396 |
0.4480 |
0.4502 |
376.75 |
0.3369 |
0.5320 |
0.5290 |
0.3282 |
372.75 |
0.4085 |
0.4317 |
0.6228 |
0.2057 |
370.35 |
0.4765 |
0.3365 |
0.6560 |
0.1366 |
367.35 |
0.5452 |
0.2413 |
0.6835 |
0.0822 |
367.35 |
0.5452 |
0.2413 |
0.6862 |
0.0857 |
380.35 |
0.2372 |
0.7030 |
0.3970 |
0.5369 |
375.45 |
0.3696 |
0.5380 |
0.5466 |
0.3339 |
372.45 |
0.4581 |
0.4281 |
0.6169 |
0.2293 |
372.45 |
0.5368 |
0.3296 |
0.6884 |
0.1709 |
366.45 |
0.6625 |
0.1726 |
0.7019 |
0.0733 |
367.95 |
0.5994 |
0.2518 |
0.7065 |
0.0953 |
383.95 |
0.0985 |
0.8773 |
0.1898 |
0.7858 |
383.15 |
0.1546 |
0.8071 |
0.2671 |
0.6906 |
378.15 |
0.2932 |
0.6341 |
0.4796 |
0.4414 |
387.85 |
0.0328 |
0.9596 |
0.0582 |
0.9308 |
386.95 |
0.0584 |
0.9255 |
0.1097 |
0.8718 |
385.25 |
0.0985 |
0.8773 |
0.1749 |
0.7961 |
387.85 |
0.0359 |
0.9596 |
0.0457 |
0.9422 |
385.85 |
0.0914 |
0.8983 |
0.1381 |
0.8434 |
383.15 |
0.1571 |
0.8251 |
0.2144 |
0.7519 |
375.35 |
0.4420 |
0.5085 |
0.5884 |
0.3278 |
380.95 |
0.2473 |
0.7250 |
0.3879 |
0.5775 |
372.15 |
0.5568 |
0.3810 |
0.6718 |
0.2035 |
367.75 |
0.6905 |
0.2325 |
0.7023 |
0.0949 |
365.75 |
0.7935 |
0.1185 |
0.7100 |
0.0474 |
387.95 |
0.0359 |
0.9596 |
0.0643 |
0.9252 |
385.75 |
0.0914 |
0.8983 |
0.1725 |
0.8132 |
383.75 |
0.1571 |
0.8251 |
0.2099 |
0.7534 |
381.55 |
0.2473 |
0.7250 |
0.3941 |
0.5694 |
383.35 |
0.1571 |
0.8251 |
0.1954 |
0.7631 |
382.45 |
0.1946 |
0.7830 |
0.3306 |
0.6428 |
378.75 |
0.3401 |
0.6220 |
0.4975 |
0.4465 |
383.35 |
0.1571 |
0.8251 |
0.2389 |
0.7281 |
387.35 |
0.0359 |
0.9596 |
0.0706 |
0.9165 |
385.55 |
0.0914 |
0.8983 |
0.1754 |
0.8090 |
383.95 |
0.1571 |
0.8251 |
0.2076 |
0.7547 |
365.85 |
0.5158 |
0.1761 |
0.7171 |
0.0534 |
365.55 |
0.7204 |
0.1155 |
0.7192 |
0.0397 |
366.55 |
0.8968 |
0.0691 |
0.7488 |
0.0339 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Water (3) - Liquid |
x2[mol/mol] of Acetic acid (2) - Liquid |
y1[mol/mol] of Water (3) - Vapour |
y2[mol/mol] of Acetic acid (2) - Vapour |
384.55 |
0.7215 |
0.0979 |
0.6213 |
0.2311 |
380.85 |
0.6622 |
0.1754 |
0.4656 |
0.4147 |
376.05 |
0.5415 |
0.3271 |
0.3122 |
0.5710 |
374.45 |
0.4784 |
0.4208 |
0.2476 |
0.6573 |
376.95 |
0.5690 |
0.3524 |
0.3625 |
0.5408 |
378.25 |
0.6082 |
0.3187 |
0.4228 |
0.4924 |
378.65 |
0.6248 |
0.2850 |
0.4395 |
0.4638 |
379.45 |
0.6468 |
0.2471 |
0.4633 |
0.4305 |
380.25 |
0.6590 |
0.2042 |
0.4844 |
0.3896 |
381.75 |
0.6720 |
0.1604 |
0.5246 |
0.3320 |
382.35 |
0.6563 |
0.1324 |
0.5189 |
0.3120 |
383.05 |
0.6321 |
0.1154 |
0.5030 |
0.3017 |
384.15 |
0.6051 |
0.0941 |
0.5043 |
0.2680 |
385.65 |
0.5717 |
0.0766 |
0.4962 |
0.2358 |
Sources