Operational condition: Pressure, kPa = 101.3 (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 |
298.15 | 0.9989 | 0.0000 | 0.0000 | 0.0904 |
298.15 | 0.9707 | 0.0279 | 0.0660 | 0.1443 |
298.15 | 0.9416 | 0.0563 | 0.1342 | 0.2010 |
298.15 | 0.9117 | 0.0843 | 0.1909 | 0.2587 |
298.15 | 0.8904 | 0.1053 | 0.2254 | 0.2997 |
298.15 | 0.8480 | 0.1402 | 0.2624 | 0.3873 |
298.15 | 0.8197 | 0.1633 | 0.2746 | 0.4490 |
298.15 | 0.7764 | 0.1944 | 0.2708 | 0.5382 |
303.15 | 0.9991 | 0.0000 | 0.0000 | 0.1122 |
303.15 | 0.9717 | 0.0268 | 0.0633 | 0.1512 |
303.15 | 0.9475 | 0.0501 | 0.1183 | 0.1891 |
303.15 | 0.9221 | 0.0743 | 0.1685 | 0.2410 |
303.15 | 0.8970 | 0.0989 | 0.2127 | 0.2939 |
303.15 | 0.8708 | 0.1217 | 0.2428 | 0.3383 |
303.15 | 0.8450 | 0.1451 | 0.2642 | 0.3921 |
303.15 | 0.8028 | 0.1766 | 0.2779 | 0.4657 |
308.15 | 0.9991 | 0.0000 | 0.0000 | 0.1053 |
308.15 | 0.9699 | 0.0286 | 0.0684 | 0.1577 |
308.15 | 0.9400 | 0.0579 | 0.1358 | 0.2168 |
308.15 | 0.9097 | 0.0868 | 0.1942 | 0.2723 |
308.15 | 0.8846 | 0.1093 | 0.2259 | 0.3143 |
308.15 | 0.8578 | 0.1316 | 0.2593 | 0.3923 |
308.15 | 0.8073 | 0.1740 | 0.2729 | 0.4662 |
308.15 | 0.7626 | 0.2011 | 0.2674 | 0.5568 |
313.15 | 0.9992 | 0.0000 | 0.0000 | 0.1119 |
313.15 | 0.9680 | 0.0309 | 0.0706 | 0.1661 |
313.15 | 0.9384 | 0.0593 | 0.1418 | 0.2263 |
313.15 | 0.9163 | 0.0800 | 0.1840 | 0.2689 |
313.15 | 0.8829 | 0.1121 | 0.2294 | 0.3292 |
313.15 | 0.8581 | 0.1306 | 0.2515 | 0.3734 |
313.15 | 0.8475 | 0.1381 | 0.2555 | 0.3935 |
313.15 | 0.7730 | 0.1949 | 0.2720 | 0.5238 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Acetic acid (2) - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Acetic acid (2) - Gas |
377.05 | 0.6636 | 0.2438 | 0.4274 | 0.4329 |
377.75 | 0.6687 | 0.2562 | 0.4246 | 0.4608 |
379.05 | 0.7068 | 0.2184 | 0.3888 | 0.4979 |
379.65 | 0.7350 | 0.1927 | 0.3559 | 0.5327 |
380.25 | 0.7582 | 0.1729 | 0.3337 | 0.5565 |
381.35 | 0.7831 | 0.1533 | 0.3004 | 0.5861 |
383.27 | 0.8214 | 0.1278 | 0.2916 | 0.6706 |
377.25 | 0.6611 | 0.2397 | 0.4278 | 0.4195 |
377.65 | 0.6742 | 0.2322 | 0.4273 | 0.4066 |
379.05 | 0.7146 | 0.2056 | 0.3945 | 0.4681 |
374.75 | 0.5146 | 0.4352 | 0.5819 | 0.3155 |
375.05 | 0.5217 | 0.4300 | 0.5706 | 0.3325 |
375.55 | 0.5821 | 0.3493 | 0.5163 | 0.3640 |
376.45 | 0.6121 | 0.3177 | 0.4863 | 0.3962 |
377.05 | 0.6445 | 0.2817 | 0.4534 | 0.4301 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of sec-Butyl acetate (1) - Liquid mixture 1 | Mole fraction of Acetic acid (2) - Liquid mixture 1 | Mole fraction of sec-Butyl acetate (1) - Liquid mixture 2 | Mole fraction of Acetic acid (2) - Liquid mixture 2 |
283.15 | 0.9440 | 0.0000 | 0.0010 | 0.0000 |
283.15 | 0.8840 | 0.0270 | 0.0020 | 0.0090 |
283.15 | 0.8240 | 0.0570 | 0.0020 | 0.0180 |
283.15 | 0.7860 | 0.0870 | 0.0020 | 0.0270 |
283.15 | 0.7280 | 0.1250 | 0.0030 | 0.0410 |
283.15 | 0.6770 | 0.1570 | 0.0030 | 0.0530 |
283.15 | 0.6270 | 0.1830 | 0.0040 | 0.0630 |
283.15 | 0.5760 | 0.2120 | 0.0040 | 0.0810 |
283.15 | 0.5330 | 0.2330 | 0.0040 | 0.0920 |
283.15 | 0.4850 | 0.2520 | 0.0060 | 0.1080 |
283.15 | 0.4280 | 0.2740 | 0.0070 | 0.1280 |
283.15 | 0.4060 | 0.2810 | 0.0090 | 0.1380 |
283.15 | 0.3660 | 0.2920 | 0.0110 | 0.1560 |
283.15 | 0.3280 | 0.2970 | 0.0130 | 0.1710 |
283.15 | 0.2380 | 0.2820 | 0.0210 | 0.1930 |
283.15 | 0.1980 | 0.2880 | 0.0310 | 0.2120 |
283.15 | 0.1890 | 0.2830 | 0.0290 | 0.2010 |
283.15 | 0.1340 | 0.2680 | 0.0510 | 0.2240 |
323.15 | 0.9060 | 0.0000 | 0.0010 | 0.0000 |
323.15 | 0.8560 | 0.0310 | 0.0010 | 0.0100 |
323.15 | 0.8010 | 0.0550 | 0.0020 | 0.0170 |
323.15 | 0.7580 | 0.0930 | 0.0020 | 0.0290 |
323.15 | 0.6960 | 0.1280 | 0.0020 | 0.0420 |
323.15 | 0.6660 | 0.1430 | 0.0020 | 0.0520 |
323.15 | 0.5100 | 0.2250 | 0.0040 | 0.0860 |
323.15 | 0.4810 | 0.2480 | 0.0060 | 0.1130 |
323.15 | 0.4160 | 0.2570 | 0.0070 | 0.1330 |
323.15 | 0.3890 | 0.2700 | 0.0090 | 0.1440 |
323.15 | 0.3380 | 0.2850 | 0.0120 | 0.1640 |
323.15 | 0.2920 | 0.2770 | 0.0180 | 0.1770 |
323.15 | 0.2490 | 0.2810 | 0.0230 | 0.1970 |
323.15 | 0.2010 | 0.2730 | 0.0370 | 0.2130 |
323.15 | 0.5800 | 0.1810 | 0.0030 | 0.0680 |
323.15 | 0.5200 | 0.2240 | 0.0040 | 0.0840 |
Operational condition: Pressure, kPa = 101.3 (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 |
298.15 | 0.9989 | 0.0000 | 0.0000 | 0.0904 |
298.15 | 0.9707 | 0.0279 | 0.0660 | 0.1443 |
298.15 | 0.9416 | 0.0563 | 0.1342 | 0.2010 |
298.15 | 0.9117 | 0.0843 | 0.1909 | 0.2587 |
298.15 | 0.8904 | 0.1053 | 0.2254 | 0.2997 |
298.15 | 0.8480 | 0.1402 | 0.2624 | 0.3873 |
298.15 | 0.8197 | 0.1633 | 0.2746 | 0.4490 |
298.15 | 0.7764 | 0.1944 | 0.2708 | 0.5382 |
303.15 | 0.9991 | 0.0000 | 0.0000 | 0.1122 |
303.15 | 0.9717 | 0.0268 | 0.0633 | 0.1512 |
303.15 | 0.9475 | 0.0501 | 0.1183 | 0.1891 |
303.15 | 0.9221 | 0.0743 | 0.1685 | 0.2410 |
303.15 | 0.8970 | 0.0989 | 0.2127 | 0.2939 |
303.15 | 0.8708 | 0.1217 | 0.2428 | 0.3383 |
303.15 | 0.8450 | 0.1451 | 0.2642 | 0.3921 |
303.15 | 0.8028 | 0.1766 | 0.2779 | 0.4657 |
308.15 | 0.9991 | 0.0000 | 0.0000 | 0.1053 |
308.15 | 0.9699 | 0.0286 | 0.0684 | 0.1577 |
308.15 | 0.9400 | 0.0579 | 0.1358 | 0.2168 |
308.15 | 0.9097 | 0.0868 | 0.1942 | 0.2723 |
308.15 | 0.8846 | 0.1093 | 0.2259 | 0.3143 |
308.15 | 0.8578 | 0.1316 | 0.2593 | 0.3923 |
308.15 | 0.8073 | 0.1740 | 0.2729 | 0.4662 |
308.15 | 0.7626 | 0.2011 | 0.2674 | 0.5568 |
313.15 | 0.9992 | 0.0000 | 0.0000 | 0.1119 |
313.15 | 0.9680 | 0.0309 | 0.0706 | 0.1661 |
313.15 | 0.9384 | 0.0593 | 0.1418 | 0.2263 |
313.15 | 0.9163 | 0.0800 | 0.1840 | 0.2689 |
313.15 | 0.8829 | 0.1121 | 0.2294 | 0.3292 |
313.15 | 0.8581 | 0.1306 | 0.2515 | 0.3734 |
313.15 | 0.8475 | 0.1381 | 0.2555 | 0.3935 |
313.15 | 0.7730 | 0.1949 | 0.2720 | 0.5238 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Acetic acid (2) - Liquid | Mole fraction of Water (3) - Liquid | Mole fraction of Water (3) - Gas | Mole fraction of Acetic acid (2) - Gas |
377.05 | 0.6636 | 0.2438 | 0.4274 | 0.4329 |
377.75 | 0.6687 | 0.2562 | 0.4246 | 0.4608 |
379.05 | 0.7068 | 0.2184 | 0.3888 | 0.4979 |
379.65 | 0.7350 | 0.1927 | 0.3559 | 0.5327 |
380.25 | 0.7582 | 0.1729 | 0.3337 | 0.5565 |
381.35 | 0.7831 | 0.1533 | 0.3004 | 0.5861 |
383.27 | 0.8214 | 0.1278 | 0.2916 | 0.6706 |
377.25 | 0.6611 | 0.2397 | 0.4278 | 0.4195 |
377.65 | 0.6742 | 0.2322 | 0.4273 | 0.4066 |
379.05 | 0.7146 | 0.2056 | 0.3945 | 0.4681 |
374.75 | 0.5146 | 0.4352 | 0.5819 | 0.3155 |
375.05 | 0.5217 | 0.4300 | 0.5706 | 0.3325 |
375.55 | 0.5821 | 0.3493 | 0.5163 | 0.3640 |
376.45 | 0.6121 | 0.3177 | 0.4863 | 0.3962 |
377.05 | 0.6445 | 0.2817 | 0.4534 | 0.4301 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of sec-Butyl acetate (1) - Liquid mixture 1 | Mole fraction of Acetic acid (2) - Liquid mixture 1 | Mole fraction of sec-Butyl acetate (1) - Liquid mixture 2 | Mole fraction of Acetic acid (2) - Liquid mixture 2 |
283.15 | 0.9440 | 0.0000 | 0.0010 | 0.0000 |
283.15 | 0.8840 | 0.0270 | 0.0020 | 0.0090 |
283.15 | 0.8240 | 0.0570 | 0.0020 | 0.0180 |
283.15 | 0.7860 | 0.0870 | 0.0020 | 0.0270 |
283.15 | 0.7280 | 0.1250 | 0.0030 | 0.0410 |
283.15 | 0.6770 | 0.1570 | 0.0030 | 0.0530 |
283.15 | 0.6270 | 0.1830 | 0.0040 | 0.0630 |
283.15 | 0.5760 | 0.2120 | 0.0040 | 0.0810 |
283.15 | 0.5330 | 0.2330 | 0.0040 | 0.0920 |
283.15 | 0.4850 | 0.2520 | 0.0060 | 0.1080 |
283.15 | 0.4280 | 0.2740 | 0.0070 | 0.1280 |
283.15 | 0.4060 | 0.2810 | 0.0090 | 0.1380 |
283.15 | 0.3660 | 0.2920 | 0.0110 | 0.1560 |
283.15 | 0.3280 | 0.2970 | 0.0130 | 0.1710 |
283.15 | 0.2380 | 0.2820 | 0.0210 | 0.1930 |
283.15 | 0.1980 | 0.2880 | 0.0310 | 0.2120 |
283.15 | 0.1890 | 0.2830 | 0.0290 | 0.2010 |
283.15 | 0.1340 | 0.2680 | 0.0510 | 0.2240 |
323.15 | 0.9060 | 0.0000 | 0.0010 | 0.0000 |
323.15 | 0.8560 | 0.0310 | 0.0010 | 0.0100 |
323.15 | 0.8010 | 0.0550 | 0.0020 | 0.0170 |
323.15 | 0.7580 | 0.0930 | 0.0020 | 0.0290 |
323.15 | 0.6960 | 0.1280 | 0.0020 | 0.0420 |
323.15 | 0.6660 | 0.1430 | 0.0020 | 0.0520 |
323.15 | 0.5100 | 0.2250 | 0.0040 | 0.0860 |
323.15 | 0.4810 | 0.2480 | 0.0060 | 0.1130 |
323.15 | 0.4160 | 0.2570 | 0.0070 | 0.1330 |
323.15 | 0.3890 | 0.2700 | 0.0090 | 0.1440 |
323.15 | 0.3380 | 0.2850 | 0.0120 | 0.1640 |
323.15 | 0.2920 | 0.2770 | 0.0180 | 0.1770 |
323.15 | 0.2490 | 0.2810 | 0.0230 | 0.1970 |
323.15 | 0.2010 | 0.2730 | 0.0370 | 0.2130 |
323.15 | 0.5800 | 0.1810 | 0.0030 | 0.0680 |
323.15 | 0.5200 | 0.2240 | 0.0040 | 0.0840 |