Mixture of 1-Butanol + Acetic acid, butyl ester

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1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

Acetic acid, butyl ester

Name
Acetic acid, butyl ester
InChI
InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key
DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCOC(C)=O
Mol. Weight (g/mol)
116.16
CAS
123-86-4
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Datasets

  1. Mole fraction (6)
  2. ρl - Mass density, kg/m3 (2)
  3. Tboil - Boiling temperature at pressure P, K (8)
  4. Vapor Liquid Equilibrium at Constant Pressure (3)

Mole fraction of Acetic acid, butyl ester (2) [ref]

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

Mole fraction of 1-Butanol (1) [ref]

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

Mole fraction of 1-Butanol (1) [ref]

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

Mole fraction of Acetic acid, butyl ester (2) [ref]

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

Mole fraction of 1-Butanol (1) [ref]

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

Mole fraction of 1-Butanol (1) [ref]

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

Mass density, kg/m3 [ref]

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

Mass density, kg/m3 [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Boiling temperature at pressure P, K [ref]

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

Vapor Liquid Equilibrium at Constant Pressure [ref]

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

Vapor Liquid Equilibrium at Constant Pressure [ref]

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

Vapor Liquid Equilibrium at Constant Pressure [ref]

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

Sources