Mixture of 1-Propanol + Di-n-propyl ether + Ethanol, 2-ethoxy-

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

Ethanol, 2-ethoxy-

Name
Ethanol, 2-ethoxy-
InChI
InChI=1S/C4H10O2/c1-2-6-4-3-5/h5H,2-4H2,1H3
InChI Key
ZNQVEEAIQZEUHB-UHFFFAOYSA-N
Formula
C4H10O2
SMILES
CCOCCO
Mol. Weight (g/mol)
90.12
CAS
110-80-5
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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 Di-n-propyl ether (2) - Liquid Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas Mole fraction of Di-n-propyl ether (2) - Gas
359.12 0.4500 0.4960 0.6030 0.3780
359.19 0.2390 0.7050 0.7100 0.2650
359.55 0.3010 0.6090 0.6760 0.2930
359.78 0.4060 0.5050 0.6200 0.3520
360.07 0.1960 0.7100 0.7380 0.2250
360.54 0.5110 0.3990 0.5600 0.4150
360.98 0.6650 0.2870 0.4790 0.5060
361.37 0.0930 0.8120 0.8200 0.1340
361.68 0.6130 0.2930 0.4940 0.4820
361.82 0.3140 0.4890 0.6560 0.2920
362.01 0.0470 0.9010 0.8820 0.0830
362.04 0.2010 0.5980 0.7260 0.2130
363.08 0.0970 0.7120 0.8040 0.1230
363.58 0.7090 0.1940 0.4030 0.5760
364.12 0.2040 0.5030 0.7100 0.2090
364.33 0.4610 0.3070 0.5430 0.4030
364.57 0.3090 0.3950 0.6350 0.2910
365.24 0.5480 0.2320 0.4690 0.4810
365.28 0.0560 0.6520 0.8250 0.0740
365.53 0.4150 0.2900 0.5500 0.3800
366.40 0.1970 0.4120 0.6930 0.2040
366.54 0.1000 0.5150 0.7700 0.1150
366.73 0.8080 0.0920 0.2570 0.7230
367.10 0.3030 0.3060 0.6050 0.3000
367.65 0.5160 0.1860 0.4400 0.4920
367.91 0.9090 0.0420 0.1440 0.8470
368.15 0.6770 0.1160 0.3160 0.6400
368.98 0.4100 0.1970 0.4870 0.4160
369.19 0.0590 0.4500 0.7850 0.0720
369.65 0.2110 0.2950 0.6380 0.2290
370.92 0.6130 0.0900 0.2820 0.6450
371.28 0.7560 0.0400 0.1540 0.7960
371.67 0.3120 0.1930 0.5150 0.3520
372.65 0.1050 0.2960 0.6970 0.1290
374.29 0.2040 0.1990 0.5620 0.2520
375.08 0.5600 0.0450 0.1920 0.6960
375.21 0.4070 0.0970 0.3370 0.5120
375.85 0.0600 0.2390 0.6840 0.0830
379.69 0.3620 0.0580 0.2580 0.5370
380.22 0.2210 0.1040 0.4080 0.3350
387.74 0.0850 0.0820 0.4100 0.1670

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 (2) - Liquid Mole fraction of 1-Propanol (1) - Liquid Mole fraction of 1-Propanol (1) - Gas Mole fraction of Di-n-propyl ether (2) - Gas
359.12 0.4500 0.4960 0.6030 0.3780
359.19 0.2390 0.7050 0.7100 0.2650
359.55 0.3010 0.6090 0.6760 0.2930
359.78 0.4060 0.5050 0.6200 0.3520
360.07 0.1960 0.7100 0.7380 0.2250
360.54 0.5110 0.3990 0.5600 0.4150
360.98 0.6650 0.2870 0.4790 0.5060
361.37 0.0930 0.8120 0.8200 0.1340
361.68 0.6130 0.2930 0.4940 0.4820
361.82 0.3140 0.4890 0.6560 0.2920
362.01 0.0470 0.9010 0.8820 0.0830
362.04 0.2010 0.5980 0.7260 0.2130
363.08 0.0970 0.7120 0.8040 0.1230
363.58 0.7090 0.1940 0.4030 0.5760
364.12 0.2040 0.5030 0.7100 0.2090
364.33 0.4610 0.3070 0.5430 0.4030
364.57 0.3090 0.3950 0.6350 0.2910
365.24 0.5480 0.2320 0.4690 0.4810
365.28 0.0560 0.6520 0.8250 0.0740
365.53 0.4150 0.2900 0.5500 0.3800
366.40 0.1970 0.4120 0.6930 0.2040
366.54 0.1000 0.5150 0.7700 0.1150
366.73 0.8080 0.0920 0.2570 0.7230
367.10 0.3030 0.3060 0.6050 0.3000
367.65 0.5160 0.1860 0.4400 0.4920
367.91 0.9090 0.0420 0.1440 0.8470
368.15 0.6770 0.1160 0.3160 0.6400
368.98 0.4100 0.1970 0.4870 0.4160
369.19 0.0590 0.4500 0.7850 0.0720
369.65 0.2110 0.2950 0.6380 0.2290
370.92 0.6130 0.0900 0.2820 0.6450
371.28 0.7560 0.0400 0.1540 0.7960
371.67 0.3120 0.1930 0.5150 0.3520
372.65 0.1050 0.2960 0.6970 0.1290
374.29 0.2040 0.1990 0.5620 0.2520
375.08 0.5600 0.0450 0.1920 0.6960
375.21 0.4070 0.0970 0.3370 0.5120
375.85 0.0600 0.2390 0.6840 0.0830
379.69 0.3620 0.0580 0.2580 0.5370
380.22 0.2210 0.1040 0.4080 0.3350
387.74 0.0850 0.0820 0.4100 0.1670

Sources