Mixture of 1-Propanol + 1,2-Ethanediol + 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

1,2-Ethanediol

Name
1,2-Ethanediol
InChI
InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
InChI Key
LYCAIKOWRPUZTN-UHFFFAOYSA-N
Formula
C2H6O2
SMILES
OCCO
Mol. Weight (g/mol)
62.07
CAS
107-21-1

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Temperature, K x Mole fraction (2)

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Di-n-propyl ether (3) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of Di-n-propyl ether (3) - Liquid mixture 2
283.15 0.9910 0.0000 0.0000 0.0050
283.15 0.9270 0.0590 0.0820 0.0130
283.15 0.9070 0.0750 0.1020 0.0170
283.15 0.8990 0.0830 0.1100 0.0190
283.15 0.8640 0.1080 0.1350 0.0240
283.15 0.8340 0.1290 0.1620 0.0310
283.15 0.8160 0.1430 0.1690 0.0380
283.15 0.7880 0.1600 0.1890 0.0390
283.15 0.7770 0.1690 0.1950 0.0460
283.15 0.7500 0.1860 0.2090 0.0530
283.15 0.7350 0.1940 0.2170 0.0560
283.15 0.7060 0.2110 0.2360 0.0600
283.15 0.6700 0.2300 0.2450 0.0730
283.15 0.6470 0.2410 0.2610 0.0770
283.15 0.6230 0.2500 0.2740 0.0870
283.15 0.5900 0.2650 0.2840 0.0950
283.15 0.5600 0.2770 0.2860 0.1110
283.15 0.5400 0.2900 0.2940 0.1210
283.15 0.4880 0.3000 0.3070 0.1500
283.15 0.4600 0.3120 0.3180 0.1570
283.15 0.4130 0.3170 0.3230 0.1830
323.15 0.9900 0.0000 0.0000 0.0060
323.15 0.9720 0.0160 0.0190 0.0100
323.15 0.9500 0.0320 0.0380 0.0110
323.15 0.9280 0.0500 0.0570 0.0140
323.15 0.9040 0.0690 0.0760 0.0180
323.15 0.8810 0.0870 0.0960 0.0220
323.15 0.8660 0.0950 0.1030 0.0230
323.15 0.8320 0.1220 0.1270 0.0280
323.15 0.7970 0.1430 0.1470 0.0340
323.15 0.7760 0.1560 0.1590 0.0430
323.15 0.7420 0.1760 0.1760 0.0450
323.15 0.7280 0.1840 0.1900 0.0510
323.15 0.6970 0.2010 0.1970 0.0560
323.15 0.6780 0.2110 0.2160 0.0630
323.15 0.6470 0.2260 0.2250 0.0710
323.15 0.6070 0.2420 0.2490 0.0880
323.15 0.5760 0.2560 0.2580 0.0960
323.15 0.5480 0.2680 0.2670 0.1090
323.15 0.5060 0.2830 0.2790 0.1230
323.15 0.4570 0.2930 0.2880 0.1460
323.15 0.4080 0.2940 0.2900 0.1770
323.15 0.3750 0.3090 0.3110 0.2670

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Di-n-propyl ether (3) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of Di-n-propyl ether (3) - Liquid mixture 2
283.15 0.9910 0.0000 0.0000 0.0050
283.15 0.9270 0.0590 0.0820 0.0130
283.15 0.9070 0.0750 0.1020 0.0170
283.15 0.8990 0.0830 0.1100 0.0190
283.15 0.8640 0.1080 0.1350 0.0240
283.15 0.8340 0.1290 0.1620 0.0310
283.15 0.8160 0.1430 0.1690 0.0380
283.15 0.7880 0.1600 0.1890 0.0390
283.15 0.7770 0.1690 0.1950 0.0460
283.15 0.7500 0.1860 0.2090 0.0530
283.15 0.7350 0.1940 0.2170 0.0560
283.15 0.7060 0.2110 0.2360 0.0600
283.15 0.6700 0.2300 0.2450 0.0730
283.15 0.6470 0.2410 0.2610 0.0770
283.15 0.6230 0.2500 0.2740 0.0870
283.15 0.5900 0.2650 0.2840 0.0950
283.15 0.5600 0.2770 0.2860 0.1110
283.15 0.5400 0.2900 0.2940 0.1210
283.15 0.4880 0.3000 0.3070 0.1500
283.15 0.4600 0.3120 0.3180 0.1570
283.15 0.4130 0.3170 0.3230 0.1830
323.15 0.9900 0.0000 0.0000 0.0060
323.15 0.9720 0.0160 0.0190 0.0100
323.15 0.9500 0.0320 0.0380 0.0110
323.15 0.9280 0.0500 0.0570 0.0140
323.15 0.9040 0.0690 0.0760 0.0180
323.15 0.8810 0.0870 0.0960 0.0220
323.15 0.8660 0.0950 0.1030 0.0230
323.15 0.8320 0.1220 0.1270 0.0280
323.15 0.7970 0.1430 0.1470 0.0340
323.15 0.7760 0.1560 0.1590 0.0430
323.15 0.7420 0.1760 0.1760 0.0450
323.15 0.7280 0.1840 0.1900 0.0510
323.15 0.6970 0.2010 0.1970 0.0560
323.15 0.6780 0.2110 0.2160 0.0630
323.15 0.6470 0.2260 0.2250 0.0710
323.15 0.6070 0.2420 0.2490 0.0880
323.15 0.5760 0.2560 0.2580 0.0960
323.15 0.5480 0.2680 0.2670 0.1090
323.15 0.5060 0.2830 0.2790 0.1230
323.15 0.4570 0.2930 0.2880 0.1460
323.15 0.4080 0.2940 0.2900 0.1770
323.15 0.3750 0.3090 0.3110 0.2670

Sources