Operational condition: Pressure, kPa = 150 (Liquid)
Mole fraction of Acetic acid, butyl ester (2) - Liquid | Mole fraction of Acetic acid, butyl ester (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0080 | 0.0110 |
0.0210 | 0.0260 |
0.0380 | 0.0440 |
0.0600 | 0.0680 |
0.0790 | 0.0870 |
0.1230 | 0.1290 |
0.1470 | 0.1500 |
0.1950 | 0.1900 |
0.2170 | 0.2070 |
0.2380 | 0.2250 |
0.2600 | 0.2430 |
0.2850 | 0.2640 |
0.3070 | 0.2810 |
0.3360 | 0.3030 |
0.3640 | 0.3220 |
0.3940 | 0.3420 |
0.4190 | 0.3610 |
0.4490 | 0.3860 |
0.4800 | 0.4080 |
0.5090 | 0.4320 |
0.5700 | 0.4830 |
0.5780 | 0.4870 |
0.5990 | 0.5030 |
0.6630 | 0.5490 |
0.6890 | 0.5690 |
0.7130 | 0.5910 |
0.7490 | 0.6240 |
0.7750 | 0.6510 |
0.8070 | 0.6890 |
0.8410 | 0.7370 |
0.8820 | 0.7920 |
0.9150 | 0.8480 |
0.9430 | 0.8910 |
0.9720 | 0.9470 |
0.9890 | 0.9770 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Mole fraction of 1-Butanol (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.1220 | 0.2110 |
0.1800 | 0.2720 |
0.3020 | 0.4100 |
0.4200 | 0.4910 |
0.5310 | 0.5820 |
0.6120 | 0.6520 |
0.6990 | 0.7110 |
0.7920 | 0.7910 |
0.9010 | 0.8810 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Mole fraction of 1-Butanol (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0580 | 0.1030 |
0.1160 | 0.1910 |
0.1660 | 0.2560 |
0.2200 | 0.3210 |
0.2750 | 0.3790 |
0.3250 | 0.4250 |
0.3800 | 0.4730 |
0.4300 | 0.5170 |
0.4850 | 0.5590 |
0.5410 | 0.6010 |
0.5960 | 0.6400 |
0.6510 | 0.6810 |
0.7080 | 0.7230 |
0.7560 | 0.7590 |
0.8020 | 0.7970 |
0.8470 | 0.8360 |
0.8910 | 0.8780 |
0.9330 | 0.9210 |
0.9700 | 0.9630 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 150 (Liquid)
Mole fraction of Acetic acid, butyl ester (2) - Liquid | Mole fraction of Acetic acid, butyl ester (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0080 | 0.0110 |
0.0210 | 0.0260 |
0.0380 | 0.0440 |
0.0600 | 0.0680 |
0.0790 | 0.0870 |
0.1230 | 0.1290 |
0.1470 | 0.1500 |
0.1950 | 0.1900 |
0.2170 | 0.2070 |
0.2380 | 0.2250 |
0.2600 | 0.2430 |
0.2850 | 0.2640 |
0.3070 | 0.2810 |
0.3360 | 0.3030 |
0.3640 | 0.3220 |
0.3940 | 0.3420 |
0.4190 | 0.3610 |
0.4490 | 0.3860 |
0.4800 | 0.4080 |
0.5090 | 0.4320 |
0.5700 | 0.4830 |
0.5780 | 0.4870 |
0.5990 | 0.5030 |
0.6630 | 0.5490 |
0.6890 | 0.5690 |
0.7130 | 0.5910 |
0.7490 | 0.6240 |
0.7750 | 0.6510 |
0.8070 | 0.6890 |
0.8410 | 0.7370 |
0.8820 | 0.7920 |
0.9150 | 0.8480 |
0.9430 | 0.8910 |
0.9720 | 0.9470 |
0.9890 | 0.9770 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Mole fraction of 1-Butanol (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.1220 | 0.2110 |
0.1800 | 0.2720 |
0.3020 | 0.4100 |
0.4200 | 0.4910 |
0.5310 | 0.5820 |
0.6120 | 0.6520 |
0.6990 | 0.7110 |
0.7920 | 0.7910 |
0.9010 | 0.8810 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Mole fraction of 1-Butanol (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0580 | 0.1030 |
0.1160 | 0.1910 |
0.1660 | 0.2560 |
0.2200 | 0.3210 |
0.2750 | 0.3790 |
0.3250 | 0.4250 |
0.3800 | 0.4730 |
0.4300 | 0.5170 |
0.4850 | 0.5590 |
0.5410 | 0.6010 |
0.5960 | 0.6400 |
0.6510 | 0.6810 |
0.7080 | 0.7230 |
0.7560 | 0.7590 |
0.8020 | 0.7970 |
0.8470 | 0.8360 |
0.8910 | 0.8780 |
0.9330 | 0.9210 |
0.9700 | 0.9630 |
1.0000 | 1.0000 |
Operational conditions:
Mole fraction of Acetic acid, butyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 805.9 |
0.0758 | 812.9 |
0.1018 | 815.2 |
0.1458 | 819.0 |
0.2387 | 826.7 |
0.3151 | 832.7 |
0.3468 | 835.1 |
0.3845 | 837.9 |
0.3983 | 838.9 |
0.4316 | 841.3 |
0.5002 | 846.1 |
0.5883 | 852.0 |
0.6709 | 857.3 |
0.7064 | 859.5 |
0.7919 | 864.7 |
0.8673 | 869.1 |
0.9259 | 872.4 |
0.9503 | 873.8 |
1.0000 | 876.5 |
Operational conditions:
Mole fraction of Acetic acid, butyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0000 | 805.9 |
0.0758 | 812.9 |
0.1018 | 815.2 |
0.1458 | 819.0 |
0.2387 | 826.7 |
0.3151 | 832.7 |
0.3468 | 835.1 |
0.3845 | 837.9 |
0.3983 | 838.9 |
0.4316 | 841.3 |
0.5002 | 846.1 |
0.5883 | 852.0 |
0.6709 | 857.3 |
0.7064 | 859.5 |
0.7919 | 864.7 |
0.8673 | 869.1 |
0.9259 | 872.4 |
0.9503 | 873.8 |
1.0000 | 876.5 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Gas | Boiling temperature at pressure P, K - Liquid |
---|---|
0.1020 | 399.51 |
0.1010 | 397.10 |
0.0990 | 395.61 |
0.0980 | 394.52 |
0.1020 | 393.63 |
0.1030 | 393.28 |
0.0980 | 392.99 |
0.1000 | 392.97 |
0.0980 | 393.19 |
0.1000 | 392.55 |
0.2000 | 402.78 |
0.1980 | 400.01 |
0.2030 | 398.28 |
0.2020 | 397.33 |
0.1990 | 396.39 |
0.2020 | 396.01 |
0.2020 | 395.76 |
0.2010 | 395.80 |
0.1980 | 395.89 |
0.2000 | 396.25 |
0.3000 | 406.02 |
0.3020 | 403.80 |
0.2970 | 401.87 |
0.3010 | 400.61 |
0.2970 | 399.97 |
0.2990 | 399.21 |
0.3010 | 398.63 |
0.2980 | 398.69 |
0.3010 | 398.97 |
0.3000 | 399.55 |
Operational condition: Pressure, kPa = 150 (Liquid)
Mole fraction of Acetic acid, butyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 402.59 |
0.0080 | 402.56 |
0.0210 | 402.52 |
0.0380 | 402.50 |
0.0600 | 402.47 |
0.0790 | 402.44 |
0.1230 | 402.41 |
0.1470 | 402.39 |
0.1950 | 402.42 |
0.2170 | 402.45 |
0.2380 | 402.48 |
0.2600 | 402.54 |
0.2850 | 402.60 |
0.3070 | 402.65 |
0.3360 | 402.73 |
0.3640 | 402.82 |
0.3940 | 402.94 |
0.4190 | 403.01 |
0.4490 | 403.09 |
0.4800 | 403.28 |
0.5090 | 403.47 |
0.5700 | 403.86 |
0.5780 | 403.90 |
0.5990 | 404.09 |
0.6630 | 404.64 |
0.6890 | 404.88 |
0.7130 | 405.27 |
0.7490 | 405.81 |
0.7750 | 406.24 |
0.8070 | 407.08 |
0.8410 | 407.95 |
0.8820 | 409.11 |
0.9150 | 410.13 |
0.9430 | 410.95 |
0.9720 | 412.05 |
0.9890 | 412.69 |
1.0000 | 413.30 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 399.15 |
0.1220 | 395.56 |
0.1800 | 394.31 |
0.3020 | 392.53 |
0.4200 | 391.37 |
0.5310 | 390.69 |
0.6120 | 390.38 |
0.6990 | 390.20 |
0.7920 | 390.20 |
0.9010 | 390.48 |
1.0000 | 390.48 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 399.05 |
0.0580 | 397.48 |
0.1160 | 396.08 |
0.1660 | 395.02 |
0.2200 | 393.98 |
0.2750 | 393.07 |
0.3250 | 392.34 |
0.3800 | 391.78 |
0.4300 | 391.23 |
0.4850 | 390.72 |
0.5410 | 390.44 |
0.5960 | 390.17 |
0.6510 | 389.93 |
0.7080 | 389.74 |
0.7560 | 389.54 |
0.8020 | 389.55 |
0.8470 | 389.56 |
0.8910 | 389.68 |
0.9330 | 389.83 |
0.9700 | 390.13 |
1.0000 | 390.46 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Gas | Boiling temperature at pressure P, K - Liquid |
---|---|
0.1020 | 399.51 |
0.1010 | 397.10 |
0.0990 | 395.61 |
0.0980 | 394.52 |
0.1020 | 393.63 |
0.1030 | 393.28 |
0.0980 | 392.99 |
0.1000 | 392.97 |
0.0980 | 393.19 |
0.1000 | 392.55 |
0.2000 | 402.78 |
0.1980 | 400.01 |
0.2030 | 398.28 |
0.2020 | 397.33 |
0.1990 | 396.39 |
0.2020 | 396.01 |
0.2020 | 395.76 |
0.2010 | 395.80 |
0.1980 | 395.89 |
0.2000 | 396.25 |
0.3000 | 406.02 |
0.3020 | 403.80 |
0.2970 | 401.87 |
0.3010 | 400.61 |
0.2970 | 399.97 |
0.2990 | 399.21 |
0.3010 | 398.63 |
0.2980 | 398.69 |
0.3010 | 398.97 |
0.3000 | 399.55 |
Operational condition: Pressure, kPa = 150 (Liquid)
Mole fraction of Acetic acid, butyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 402.59 |
0.0080 | 402.56 |
0.0210 | 402.52 |
0.0380 | 402.50 |
0.0600 | 402.47 |
0.0790 | 402.44 |
0.1230 | 402.41 |
0.1470 | 402.39 |
0.1950 | 402.42 |
0.2170 | 402.45 |
0.2380 | 402.48 |
0.2600 | 402.54 |
0.2850 | 402.60 |
0.3070 | 402.65 |
0.3360 | 402.73 |
0.3640 | 402.82 |
0.3940 | 402.94 |
0.4190 | 403.01 |
0.4490 | 403.09 |
0.4800 | 403.28 |
0.5090 | 403.47 |
0.5700 | 403.86 |
0.5780 | 403.90 |
0.5990 | 404.09 |
0.6630 | 404.64 |
0.6890 | 404.88 |
0.7130 | 405.27 |
0.7490 | 405.81 |
0.7750 | 406.24 |
0.8070 | 407.08 |
0.8410 | 407.95 |
0.8820 | 409.11 |
0.9150 | 410.13 |
0.9430 | 410.95 |
0.9720 | 412.05 |
0.9890 | 412.69 |
1.0000 | 413.30 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 399.15 |
0.1220 | 395.56 |
0.1800 | 394.31 |
0.3020 | 392.53 |
0.4200 | 391.37 |
0.5310 | 390.69 |
0.6120 | 390.38 |
0.6990 | 390.20 |
0.7920 | 390.20 |
0.9010 | 390.48 |
1.0000 | 390.48 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Butanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 399.05 |
0.0580 | 397.48 |
0.1160 | 396.08 |
0.1660 | 395.02 |
0.2200 | 393.98 |
0.2750 | 393.07 |
0.3250 | 392.34 |
0.3800 | 391.78 |
0.4300 | 391.23 |
0.4850 | 390.72 |
0.5410 | 390.44 |
0.5960 | 390.17 |
0.6510 | 389.93 |
0.7080 | 389.74 |
0.7560 | 389.54 |
0.8020 | 389.55 |
0.8470 | 389.56 |
0.8910 | 389.68 |
0.9330 | 389.83 |
0.9700 | 390.13 |
1.0000 | 390.46 |
Operational condition: Pressure, kPa = 101.33 (VLE)
Fixed | Measured | |
---|---|---|
T [K] - VLE | x1[mol/mol] of 1-Butanol (1) - Liquid | y1[mol/mol] of 1-Butanol (1) - Vapour |
394.9 | 0.1090 | 0.2170 |
393.25 | 0.2080 | 0.3320 |
392.25 | 0.2950 | 0.4130 |
391.55 | 0.3610 | 0.4650 |
390.95 | 0.4330 | 0.5170 |
390.65 | 0.4470 | 0.5290 |
390.45 | 0.5100 | 0.5690 |
390.25 | 0.5440 | 0.6010 |
389.95 | 0.5540 | 0.6070 |
389.75 | 0.5750 | 0.6190 |
389.55 | 0.6080 | 0.6420 |
389.45 | 0.6460 | 0.6690 |
389.35 | 0.6790 | 0.6920 |
389.35 | 0.7100 | 0.7150 |
389.75 | 0.7260 | 0.7340 |
389.35 | 0.7290 | 0.7290 |
389.7 | 0.7310 | 0.7330 |
389.7 | 0.7560 | 0.7500 |
389.45 | 0.8280 | 0.8130 |
389.95 | 0.8650 | 0.8500 |
390.15 | 0.9130 | 0.8950 |
390.15 | 0.9600 | 0.9420 |
390.15 | 0.9800 | 0.9640 |
390.15 | 0.9950 | 0.9890 |
Operational condition: Pressure, kPa = 6.666 (VLE)
Fixed | Measured | |
---|---|---|
T [K] - VLE | x1[mol/mol] of 1-Butanol (1) - Liquid | y1[mol/mol] of 1-Butanol (1) - Vapour |
325.75 | 0.0000 | 0.0000 |
324.65 | 0.1800 | 0.2250 |
324.25 | 0.2820 | 0.3220 |
323.95 | 0.3550 | 0.3630 |
323.85 | 0.3700 | 0.3700 |
323.95 | 0.4350 | 0.4160 |
324.05 | 0.4870 | 0.4370 |
324.35 | 0.5910 | 0.5040 |
325.45 | 0.7650 | 0.6450 |
326.65 | 0.8680 | 0.7520 |
327.85 | 0.9210 | 0.8330 |
329.25 | 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 22.065 (VLE)
Fixed | Measured | |
---|---|---|
T [K] - VLE | x1[mol/mol] of 1-Butanol (1) - Liquid | y1[mol/mol] of 1-Butanol (1) - Vapour |
353.65 | 0.0000 | 0.0000 |
351.35 | 0.1610 | 0.2100 |
350.05 | 0.3130 | 0.3750 |
349.55 | 0.4740 | 0.4790 |
349.65 | 0.6130 | 0.5780 |
349.95 | 0.6750 | 0.6200 |
350.35 | 0.7770 | 0.7050 |
351.45 | 0.8730 | 0.8070 |
353.45 | 1.0000 | 1.0000 |