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Mixture of Propanoic acid, butyl ester + 2-Butanone + Ethanol

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Propanoic acid, butyl ester

Name
Propanoic acid, butyl ester
InChI
InChI=1S/C7H14O2/c1-3-5-6-9-7(8)4-2/h3-6H2,1-2H3
InChI Key
BTMVHUNTONAYDX-UHFFFAOYSA-N
Formula
C7H14O2
SMILES
CCCCOC(=O)CC
Mol. Weight (g/mol)
130.18
CAS
590-01-2

2-Butanone

Name
2-Butanone
InChI
InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3
InChI Key
ZWEHNKRNPOVVGH-UHFFFAOYSA-N
Formula
C4H8O
SMILES
CCC(C)=O
Mol. Weight (g/mol)
72.11
CAS
78-93-3

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
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Datasets

  1. Temperature, K x Mole fraction (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (3) - Gas Mole fraction of 2-Butanone (2) - Gas Mole fraction of 2-Butanone (2) - Liquid Mole fraction of Ethanol (3) - Liquid
348.70 0.4710 0.5290 0.5370 0.4120
348.97 0.5950 0.4020 0.3680 0.5710
349.83 0.2860 0.7140 0.7550 0.2100
349.84 0.5660 0.4230 0.3910 0.5050
350.28 0.4090 0.5860 0.5930 0.3060
350.45 0.7270 0.2580 0.2020 0.6870
351.40 0.9110 0.0820 0.0500 0.8930
351.67 0.8380 0.1430 0.1000 0.7970
352.13 0.5420 0.4310 0.3980 0.4030
352.22 0.3140 0.6760 0.6590 0.2000
352.40 0.6290 0.3410 0.2980 0.4990
352.85 0.7220 0.2450 0.1960 0.5990
352.87 0.1820 0.8170 0.7910 0.0990
352.88 0.4550 0.5200 0.4890 0.3030
354.74 0.5990 0.3550 0.3090 0.3910
355.01 0.7020 0.2490 0.2030 0.4940
355.16 0.8730 0.0720 0.0470 0.6900
355.50 0.5070 0.4490 0.3910 0.3030
355.63 0.8090 0.1350 0.0990 0.5910
355.96 0.2010 0.7760 0.6840 0.0940
356.55 0.3730 0.5830 0.5010 0.1930
357.46 0.6640 0.2700 0.2160 0.3760
358.26 0.5720 0.3650 0.2950 0.2990
359.00 0.2230 0.7310 0.5880 0.0940
359.52 0.8380 0.0810 0.0500 0.4680
359.73 0.4150 0.5160 0.4030 0.1880
360.77 0.7470 0.1710 0.1190 0.3610
360.85 0.1280 0.8260 0.6290 0.0480
362.60 0.2460 0.6820 0.4900 0.0920
363.45 0.4650 0.4400 0.3050 0.1760
364.46 0.5700 0.3240 0.2180 0.2140
366.60 0.2720 0.6240 0.3940 0.0890
367.63 0.5320 0.3430 0.2100 0.1670
368.19 0.7590 0.1040 0.0560 0.2430
370.02 0.1540 0.7240 0.4270 0.0500
371.54 0.3030 0.5520 0.3000 0.0840
371.91 0.6200 0.2180 0.1140 0.1590
376.81 0.3630 0.4420 0.2090 0.0830
382.69 0.4490 0.2880 0.1120 0.0800
382.79 0.2080 0.5460 0.2220 0.0430
401.84 0.2750 0.1640 0.0390 0.0300

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (3) - Gas Mole fraction of 2-Butanone (2) - Gas Mole fraction of 2-Butanone (2) - Liquid Mole fraction of Ethanol (3) - Liquid
348.70 0.4710 0.5290 0.5370 0.4120
348.97 0.5950 0.4020 0.3680 0.5710
349.83 0.2860 0.7140 0.7550 0.2100
349.84 0.5660 0.4230 0.3910 0.5050
350.28 0.4090 0.5860 0.5930 0.3060
350.45 0.7270 0.2580 0.2020 0.6870
351.40 0.9110 0.0820 0.0500 0.8930
351.67 0.8380 0.1430 0.1000 0.7970
352.13 0.5420 0.4310 0.3980 0.4030
352.22 0.3140 0.6760 0.6590 0.2000
352.40 0.6290 0.3410 0.2980 0.4990
352.85 0.7220 0.2450 0.1960 0.5990
352.87 0.1820 0.8170 0.7910 0.0990
352.88 0.4550 0.5200 0.4890 0.3030
354.74 0.5990 0.3550 0.3090 0.3910
355.01 0.7020 0.2490 0.2030 0.4940
355.16 0.8730 0.0720 0.0470 0.6900
355.50 0.5070 0.4490 0.3910 0.3030
355.63 0.8090 0.1350 0.0990 0.5910
355.96 0.2010 0.7760 0.6840 0.0940
356.55 0.3730 0.5830 0.5010 0.1930
357.46 0.6640 0.2700 0.2160 0.3760
358.26 0.5720 0.3650 0.2950 0.2990
359.00 0.2230 0.7310 0.5880 0.0940
359.52 0.8380 0.0810 0.0500 0.4680
359.73 0.4150 0.5160 0.4030 0.1880
360.77 0.7470 0.1710 0.1190 0.3610
360.85 0.1280 0.8260 0.6290 0.0480
362.60 0.2460 0.6820 0.4900 0.0920
363.45 0.4650 0.4400 0.3050 0.1760
364.46 0.5700 0.3240 0.2180 0.2140
366.60 0.2720 0.6240 0.3940 0.0890
367.63 0.5320 0.3430 0.2100 0.1670
368.19 0.7590 0.1040 0.0560 0.2430
370.02 0.1540 0.7240 0.4270 0.0500
371.54 0.3030 0.5520 0.3000 0.0840
371.91 0.6200 0.2180 0.1140 0.1590
376.81 0.3630 0.4420 0.2090 0.0830
382.69 0.4490 0.2880 0.1120 0.0800
382.79 0.2080 0.5460 0.2220 0.0430
401.84 0.2750 0.1640 0.0390 0.0300

Sources