Mixture of 1-Propanol + Di-n-propyl ether + Water

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

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

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Temperature, K x Mole fraction (4)

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 (2) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of Di-n-propyl ether (2) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 2
283.15 0.9780 0.0000 0.0010 0.0000
283.15 0.9550 0.0170 0.0010 0.0090
283.15 0.9060 0.0520 0.0030 0.0220
283.15 0.8640 0.0860 0.0030 0.0290
283.15 0.7970 0.1350 0.0010 0.0360
283.15 0.7250 0.1780 0.0010 0.0410
283.15 0.6570 0.2320 0.0010 0.0440
283.15 0.5930 0.2710 0.0010 0.0480
283.15 0.5500 0.2940 0.0010 0.0490
283.15 0.4710 0.3380 0.0010 0.0520
283.15 0.4250 0.3630 0.0040 0.0570
283.15 0.3740 0.3830 0.0010 0.0560
283.15 0.3350 0.4010 0.0010 0.0570
283.15 0.3030 0.4010 0.0020 0.0580
283.15 0.1880 0.4200 0.0010 0.0660
283.15 0.1770 0.4260 0.0020 0.0680
283.15 0.1500 0.4190 0.0010 0.0700
283.15 0.1080 0.3960 0.0020 0.0810
283.15 0.0890 0.3810 0.0030 0.0920
283.15 0.0570 0.3350 0.0030 0.0990
283.15 0.0460 0.3100 0.0040 0.1060
283.15 0.0410 0.2960 0.0040 0.1020
323.15 0.9780 0.0000 0.0000 0.0000
323.15 0.9280 0.0290 0.0000 0.0060
323.15 0.8710 0.0790 0.0000 0.0150
323.15 0.8130 0.1220 0.0000 0.0190
323.15 0.7490 0.1660 0.0010 0.0240
323.15 0.7430 0.1740 0.0000 0.0240
323.15 0.6710 0.2130 0.0010 0.0280
323.15 0.6090 0.2520 0.0010 0.0300
323.15 0.5480 0.2900 0.0000 0.0320
323.15 0.5190 0.3080 0.0010 0.0350
323.15 0.4540 0.3410 0.0010 0.0370
323.15 0.4380 0.3520 0.0000 0.0360
323.15 0.3730 0.3790 0.0010 0.0400
323.15 0.3520 0.3910 0.0000 0.0400
323.15 0.3450 0.3910 0.0010 0.0420
323.15 0.3020 0.4040 0.0010 0.0440
323.15 0.2930 0.4110 0.0010 0.0440
323.15 0.2440 0.4130 0.0010 0.0480
323.15 0.2010 0.4110 0.0010 0.0510
323.15 0.1890 0.4180 0.0010 0.0520
323.15 0.1730 0.4100 0.0010 0.0530
323.15 0.1710 0.4160 0.0010 0.0520
323.15 0.1600 0.4140 0.0010 0.0530
323.15 0.1330 0.4050 0.0010 0.0560
323.15 0.0960 0.3820 0.0020 0.0690
323.15 0.0900 0.3690 0.0010 0.0670
323.15 0.0760 0.3490 0.0020 0.0700

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Fixed Measured
Temperature, K - Gas Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Gas Mole fraction of Di-n-propyl ether (2) - Liquid mixture 1 Mole fraction of Di-n-propyl ether (2) - Liquid mixture 2 Mole fraction of Di-n-propyl ether (2) - Gas
352.13 0.2440 0.1000 0.2390 0.0300 0.0050 0.3140
350.73 0.3580 0.0630 0.2180 0.0950 0.0020 0.3550
349.73 0.3990 0.0530 0.2020 0.1710 0.0010 0.3900
348.80 0.3950 0.0440 0.1820 0.2780 0.0010 0.4220
348.45 0.3910 0.0400 0.1730 0.3650 0.0000 0.4370
348.07 0.3540 0.0380 0.1620 0.4420 0.0000 0.4550
347.83 0.3200 0.0350 0.1510 0.5330 0.0000 0.4670
347.52 0.2430 0.0320 0.1320 0.6630 0.0000 0.4890
347.35 0.1590 0.0220 0.1060 0.7830 0.0000 0.5150
347.58 0.0660 0.0120 0.0610 0.8910 0.0000 0.5540

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 (2) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of Di-n-propyl ether (2) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Liquid mixture 2
283.15 0.9780 0.0000 0.0010 0.0000
283.15 0.9550 0.0170 0.0010 0.0090
283.15 0.9060 0.0520 0.0030 0.0220
283.15 0.8640 0.0860 0.0030 0.0290
283.15 0.7970 0.1350 0.0010 0.0360
283.15 0.7250 0.1780 0.0010 0.0410
283.15 0.6570 0.2320 0.0010 0.0440
283.15 0.5930 0.2710 0.0010 0.0480
283.15 0.5500 0.2940 0.0010 0.0490
283.15 0.4710 0.3380 0.0010 0.0520
283.15 0.4250 0.3630 0.0040 0.0570
283.15 0.3740 0.3830 0.0010 0.0560
283.15 0.3350 0.4010 0.0010 0.0570
283.15 0.3030 0.4010 0.0020 0.0580
283.15 0.1880 0.4200 0.0010 0.0660
283.15 0.1770 0.4260 0.0020 0.0680
283.15 0.1500 0.4190 0.0010 0.0700
283.15 0.1080 0.3960 0.0020 0.0810
283.15 0.0890 0.3810 0.0030 0.0920
283.15 0.0570 0.3350 0.0030 0.0990
283.15 0.0460 0.3100 0.0040 0.1060
283.15 0.0410 0.2960 0.0040 0.1020
323.15 0.9780 0.0000 0.0000 0.0000
323.15 0.9280 0.0290 0.0000 0.0060
323.15 0.8710 0.0790 0.0000 0.0150
323.15 0.8130 0.1220 0.0000 0.0190
323.15 0.7490 0.1660 0.0010 0.0240
323.15 0.7430 0.1740 0.0000 0.0240
323.15 0.6710 0.2130 0.0010 0.0280
323.15 0.6090 0.2520 0.0010 0.0300
323.15 0.5480 0.2900 0.0000 0.0320
323.15 0.5190 0.3080 0.0010 0.0350
323.15 0.4540 0.3410 0.0010 0.0370
323.15 0.4380 0.3520 0.0000 0.0360
323.15 0.3730 0.3790 0.0010 0.0400
323.15 0.3520 0.3910 0.0000 0.0400
323.15 0.3450 0.3910 0.0010 0.0420
323.15 0.3020 0.4040 0.0010 0.0440
323.15 0.2930 0.4110 0.0010 0.0440
323.15 0.2440 0.4130 0.0010 0.0480
323.15 0.2010 0.4110 0.0010 0.0510
323.15 0.1890 0.4180 0.0010 0.0520
323.15 0.1730 0.4100 0.0010 0.0530
323.15 0.1710 0.4160 0.0010 0.0520
323.15 0.1600 0.4140 0.0010 0.0530
323.15 0.1330 0.4050 0.0010 0.0560
323.15 0.0960 0.3820 0.0020 0.0690
323.15 0.0900 0.3690 0.0010 0.0670
323.15 0.0760 0.3490 0.0020 0.0700

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Fixed Measured
Temperature, K - Gas Mole fraction of 1-Propanol (1) - Liquid mixture 1 Mole fraction of 1-Propanol (1) - Liquid mixture 2 Mole fraction of 1-Propanol (1) - Gas Mole fraction of Di-n-propyl ether (2) - Liquid mixture 1 Mole fraction of Di-n-propyl ether (2) - Liquid mixture 2 Mole fraction of Di-n-propyl ether (2) - Gas
352.13 0.2440 0.1000 0.2390 0.0300 0.0050 0.3140
350.73 0.3580 0.0630 0.2180 0.0950 0.0020 0.3550
349.73 0.3990 0.0530 0.2020 0.1710 0.0010 0.3900
348.80 0.3950 0.0440 0.1820 0.2780 0.0010 0.4220
348.45 0.3910 0.0400 0.1730 0.3650 0.0000 0.4370
348.07 0.3540 0.0380 0.1620 0.4420 0.0000 0.4550
347.83 0.3200 0.0350 0.1510 0.5330 0.0000 0.4670
347.52 0.2430 0.0320 0.1320 0.6630 0.0000 0.4890
347.35 0.1590 0.0220 0.1060 0.7830 0.0000 0.5150
347.58 0.0660 0.0120 0.0610 0.8910 0.0000 0.5540

Sources