Mixture of 1-Propanol + Propanoic acid, butyl ester + Di-n-propyl ether

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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

Di-n-propyl ether

Name
Di-n-propyl ether
InChI
InChI=1S/C6H14O/c1-3-5-7-6-4-2/h3-6H2,1-2H3
InChI Key
POLCUAVZOMRGSN-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCOCCC
Mol. Weight (g/mol)
102.17
CAS
111-43-3
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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 Di-n-propyl ether (3) - Liquid Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas Mole fraction of Di-n-propyl ether (3) - Gas
359.71 0.6760 0.2690 0.3130 0.6820
360.13 0.4680 0.4780 0.4270 0.5670
360.86 0.5970 0.3030 0.3450 0.6430
361.14 0.4920 0.4060 0.4070 0.5800
361.19 0.7030 0.1990 0.2710 0.7180
361.90 0.3870 0.5120 0.4700 0.5150
362.05 0.2770 0.6720 0.5490 0.4430
362.77 0.8920 0.0530 0.1030 0.8910
362.77 0.8020 0.0960 0.1670 0.8200
363.31 0.2770 0.6190 0.5470 0.4340
364.17 0.4920 0.3000 0.3760 0.5920
364.32 0.5960 0.1980 0.2900 0.6790
364.46 0.3870 0.4090 0.4510 0.5160
365.10 0.1830 0.7130 0.6350 0.3440
365.28 0.2870 0.5090 0.5310 0.4310
365.89 0.6960 0.0980 0.1770 0.7890
367.32 0.5040 0.1930 0.3070 0.6380
367.51 0.3990 0.2910 0.4070 0.5360
367.58 0.0910 0.8050 0.7540 0.2220
367.97 0.1420 0.6550 0.6720 0.2820
368.22 0.2980 0.3880 0.5000 0.4410
368.56 0.0320 0.9260 0.8700 0.1240
370.71 0.6450 0.0440 0.0980 0.8380
371.04 0.0400 0.7510 0.8300 0.1140
371.17 0.3960 0.1980 0.3440 0.5710
371.42 0.2950 0.2960 0.4620 0.4530
371.53 0.0960 0.5940 0.7210 0.2020
372.18 0.1970 0.3990 0.5740 0.3360
372.95 0.4950 0.0920 0.1930 0.7140
374.62 0.2870 0.2120 0.4020 0.4770
375.16 0.0520 0.5430 0.7720 0.1150
375.19 0.1900 0.3120 0.5370 0.3400
376.60 0.1020 0.3970 0.6640 0.2030
377.45 0.4430 0.0610 0.1480 0.7210
379.63 0.2090 0.1940 0.4310 0.3960
380.78 0.2990 0.1040 0.2600 0.5630
383.43 0.0520 0.3090 0.6790 0.1120
388.12 0.1010 0.1750 0.4930 0.2320
390.27 0.2280 0.0520 0.1660 0.5330
394.30 0.1070 0.0920 0.3320 0.2760
403.13 0.0580 0.0510 0.2390 0.1940

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Di-n-propyl ether (3) - Liquid Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas Mole fraction of Di-n-propyl ether (3) - Gas
359.71 0.6760 0.2690 0.3130 0.6820
360.13 0.4680 0.4780 0.4270 0.5670
360.86 0.5970 0.3030 0.3450 0.6430
361.14 0.4920 0.4060 0.4070 0.5800
361.19 0.7030 0.1990 0.2710 0.7180
361.90 0.3870 0.5120 0.4700 0.5150
362.05 0.2770 0.6720 0.5490 0.4430
362.77 0.8920 0.0530 0.1030 0.8910
362.77 0.8020 0.0960 0.1670 0.8200
363.31 0.2770 0.6190 0.5470 0.4340
364.17 0.4920 0.3000 0.3760 0.5920
364.32 0.5960 0.1980 0.2900 0.6790
364.46 0.3870 0.4090 0.4510 0.5160
365.10 0.1830 0.7130 0.6350 0.3440
365.28 0.2870 0.5090 0.5310 0.4310
365.89 0.6960 0.0980 0.1770 0.7890
367.32 0.5040 0.1930 0.3070 0.6380
367.51 0.3990 0.2910 0.4070 0.5360
367.58 0.0910 0.8050 0.7540 0.2220
367.97 0.1420 0.6550 0.6720 0.2820
368.22 0.2980 0.3880 0.5000 0.4410
368.56 0.0320 0.9260 0.8700 0.1240
370.71 0.6450 0.0440 0.0980 0.8380
371.04 0.0400 0.7510 0.8300 0.1140
371.17 0.3960 0.1980 0.3440 0.5710
371.42 0.2950 0.2960 0.4620 0.4530
371.53 0.0960 0.5940 0.7210 0.2020
372.18 0.1970 0.3990 0.5740 0.3360
372.95 0.4950 0.0920 0.1930 0.7140
374.62 0.2870 0.2120 0.4020 0.4770
375.16 0.0520 0.5430 0.7720 0.1150
375.19 0.1900 0.3120 0.5370 0.3400
376.60 0.1020 0.3970 0.6640 0.2030
377.45 0.4430 0.0610 0.1480 0.7210
379.63 0.2090 0.1940 0.4310 0.3960
380.78 0.2990 0.1040 0.2600 0.5630
383.43 0.0520 0.3090 0.6790 0.1120
388.12 0.1010 0.1750 0.4930 0.2320
390.27 0.2280 0.0520 0.1660 0.5330
394.30 0.1070 0.0920 0.3320 0.2760
403.13 0.0580 0.0510 0.2390 0.1940

Sources