Mixture of n-Hexane + Ethanol + Tetrahydropyran

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

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

Tetrahydropyran

Name
Tetrahydropyran
InChI
InChI=1S/C5H10O/c1-2-4-6-5-3-1/h1-5H2
InChI Key
DHXVGJBLRPWPCS-UHFFFAOYSA-N
Formula
C5H10O
SMILES
C1CCOCC1
Mol. Weight (g/mol)
86.13
CAS
142-68-7
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Datasets

  1. Mole fraction (4)
  2. γ - Surface tension liquid-gas, N/m (2)
  3. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Mole fraction of Ethanol (2) - Gas
0.1140 0.7730 0.2740
0.1140 0.6640 0.2520
0.1130 0.5630 0.2360
0.1120 0.4670 0.2230
0.1100 0.3750 0.2120
0.1040 0.2800 0.2010
0.1010 0.1920 0.1970
0.0970 0.1050 0.1990
0.1820 0.1030 0.2980
0.1860 0.1840 0.2850
0.1930 0.2710 0.2790
0.1980 0.3610 0.2800
0.2010 0.4630 0.2830
0.1990 0.5710 0.2880
0.1950 0.6860 0.2990
0.2950 0.5870 0.3190
0.2920 0.4880 0.3170
0.2900 0.3890 0.3180
0.2880 0.2950 0.3250
0.2850 0.2000 0.3400
0.2830 0.1090 0.3670
0.3800 0.1020 0.4130
0.3870 0.1900 0.3770
0.3930 0.2840 0.3560
0.3880 0.3960 0.3410
0.3930 0.4970 0.3370
0.4930 0.3990 0.3510
0.4680 0.2820 0.3680
0.4700 0.1940 0.3940
0.4630 0.1080 0.4350
0.5650 0.1040 0.4640
0.5770 0.1960 0.4080
0.5860 0.2950 0.3740
0.6890 0.1930 0.4130
0.6800 0.1030 0.4830
0.7950 0.1470 0.4440
0.8280 0.0740 0.5470

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Mole fraction of n-Hexane (1) - Gas
0.1140 0.7730 0.6750
0.1140 0.6640 0.6410
0.1130 0.5630 0.5990
0.1120 0.4670 0.5510
0.1100 0.3750 0.4970
0.1040 0.2800 0.4220
0.1010 0.1920 0.3320
0.0970 0.1050 0.2130
0.1820 0.1030 0.2160
0.1860 0.1840 0.3310
0.1930 0.2710 0.4180
0.1980 0.3610 0.4910
0.2010 0.4630 0.5550
0.1990 0.5710 0.6070
0.1950 0.6860 0.6490
0.2950 0.5870 0.6310
0.2920 0.4880 0.5860
0.2900 0.3890 0.5290
0.2880 0.2950 0.4580
0.2850 0.2000 0.3650
0.2830 0.1090 0.2400
0.3800 0.1020 0.2520
0.3870 0.1900 0.3800
0.3930 0.2840 0.4780
0.3880 0.3960 0.5580
0.3930 0.4970 0.6160
0.4930 0.3990 0.5990
0.4680 0.2820 0.5030
0.4700 0.1940 0.4160
0.4630 0.1080 0.2870
0.5650 0.1040 0.3100
0.5770 0.1960 0.4590
0.5860 0.2950 0.5660
0.6890 0.1930 0.5170
0.6800 0.1030 0.3610
0.7950 0.1470 0.5190
0.8280 0.0740 0.3700

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Mole fraction of Ethanol (2) - Gas
0.1140 0.7730 0.2740
0.1140 0.6640 0.2520
0.1130 0.5630 0.2360
0.1120 0.4670 0.2230
0.1100 0.3750 0.2120
0.1040 0.2800 0.2010
0.1010 0.1920 0.1970
0.0970 0.1050 0.1990
0.1820 0.1030 0.2980
0.1860 0.1840 0.2850
0.1930 0.2710 0.2790
0.1980 0.3610 0.2800
0.2010 0.4630 0.2830
0.1990 0.5710 0.2880
0.1950 0.6860 0.2990
0.2950 0.5870 0.3190
0.2920 0.4880 0.3170
0.2900 0.3890 0.3180
0.2880 0.2950 0.3250
0.2850 0.2000 0.3400
0.2830 0.1090 0.3670
0.3800 0.1020 0.4130
0.3870 0.1900 0.3770
0.3930 0.2840 0.3560
0.3880 0.3960 0.3410
0.3930 0.4970 0.3370
0.4930 0.3990 0.3510
0.4680 0.2820 0.3680
0.4700 0.1940 0.3940
0.4630 0.1080 0.4350
0.5650 0.1040 0.4640
0.5770 0.1960 0.4080
0.5860 0.2950 0.3740
0.6890 0.1930 0.4130
0.6800 0.1030 0.4830
0.7950 0.1470 0.4440
0.8280 0.0740 0.5470

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 94 (Liquid)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Mole fraction of n-Hexane (1) - Gas
0.1140 0.7730 0.6750
0.1140 0.6640 0.6410
0.1130 0.5630 0.5990
0.1120 0.4670 0.5510
0.1100 0.3750 0.4970
0.1040 0.2800 0.4220
0.1010 0.1920 0.3320
0.0970 0.1050 0.2130
0.1820 0.1030 0.2160
0.1860 0.1840 0.3310
0.1930 0.2710 0.4180
0.1980 0.3610 0.4910
0.2010 0.4630 0.5550
0.1990 0.5710 0.6070
0.1950 0.6860 0.6490
0.2950 0.5870 0.6310
0.2920 0.4880 0.5860
0.2900 0.3890 0.5290
0.2880 0.2950 0.4580
0.2850 0.2000 0.3650
0.2830 0.1090 0.2400
0.3800 0.1020 0.2520
0.3870 0.1900 0.3800
0.3930 0.2840 0.4780
0.3880 0.3960 0.5580
0.3930 0.4970 0.6160
0.4930 0.3990 0.5990
0.4680 0.2820 0.5030
0.4700 0.1940 0.4160
0.4630 0.1080 0.2870
0.5650 0.1040 0.3100
0.5770 0.1960 0.4590
0.5860 0.2950 0.5660
0.6890 0.1930 0.5170
0.6800 0.1030 0.3610
0.7950 0.1470 0.5190
0.8280 0.0740 0.3700

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0890 0.7960 0.0198
0.0860 0.6880 0.0188
0.0860 0.5780 0.0213
0.0850 0.4710 0.0209
0.0850 0.3650 0.0232
0.0840 0.2570 0.0225
0.0830 0.1550 0.0239
0.0890 0.0680 0.0236
0.1960 0.0690 0.0234
0.1940 0.1800 0.0234
0.1940 0.2940 0.0219
0.1960 0.4090 0.0207
0.1910 0.5260 0.0197
0.1920 0.6390 0.0180
0.1900 0.7450 0.0182
0.3170 0.6150 0.0169
0.3080 0.4770 0.0196
0.3030 0.3490 0.0210
0.2970 0.2210 0.0223
0.3770 0.0700 0.0226
0.2690 0.0370 0.0240
0.4030 0.0490 0.0244
0.4010 0.2000 0.0220
0.4030 0.3530 0.0192
0.4050 0.4820 0.0173
0.4040 0.5770 0.0168
0.5550 0.3900 0.0173
0.5270 0.2250 0.0219
0.5000 0.1000 0.0244
0.4780 0.0190 0.0247
0.6220 0.0500 0.0248
0.6160 0.2290 0.0211
0.6010 0.3700 0.0183
0.7340 0.1640 0.0208
0.6760 0.0430 0.0245
0.7920 0.0770 0.0219

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0890 0.7960 0.0198
0.0860 0.6880 0.0188
0.0860 0.5780 0.0213
0.0850 0.4710 0.0209
0.0850 0.3650 0.0232
0.0840 0.2570 0.0225
0.0830 0.1550 0.0239
0.0890 0.0680 0.0236
0.1960 0.0690 0.0234
0.1940 0.1800 0.0234
0.1940 0.2940 0.0219
0.1960 0.4090 0.0207
0.1910 0.5260 0.0197
0.1920 0.6390 0.0180
0.1900 0.7450 0.0182
0.3170 0.6150 0.0169
0.3080 0.4770 0.0196
0.3030 0.3490 0.0210
0.2970 0.2210 0.0223
0.3770 0.0700 0.0226
0.2690 0.0370 0.0240
0.4030 0.0490 0.0244
0.4010 0.2000 0.0220
0.4030 0.3530 0.0192
0.4050 0.4820 0.0173
0.4040 0.5770 0.0168
0.5550 0.3900 0.0173
0.5270 0.2250 0.0219
0.5000 0.1000 0.0244
0.4780 0.0190 0.0247
0.6220 0.0500 0.0248
0.6160 0.2290 0.0211
0.6010 0.3700 0.0183
0.7340 0.1640 0.0208
0.6760 0.0430 0.0245
0.7920 0.0770 0.0219

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94 (Gas)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.1140 0.7730 332.11
0.1140 0.6640 334.13
0.1130 0.5630 336.14
0.1120 0.4670 338.16
0.1100 0.3750 340.22
0.1040 0.2800 342.88
0.1010 0.1920 345.56
0.0970 0.1050 348.85
0.1820 0.1030 346.28
0.1860 0.1840 343.12
0.1930 0.2710 340.31
0.1980 0.3610 337.82
0.2010 0.4630 335.51
0.1990 0.5710 333.37
0.1950 0.6860 331.45
0.2950 0.5870 331.36
0.2920 0.4880 333.27
0.2900 0.3890 335.39
0.2880 0.2950 337.74
0.2850 0.2000 340.63
0.2830 0.1090 344.05
0.3800 0.1020 342.88
0.3870 0.1900 339.33
0.3930 0.2840 336.29
0.3880 0.3960 333.65
0.3930 0.4970 331.51
0.4930 0.3990 331.72
0.4680 0.2820 335.08
0.4700 0.1940 337.95
0.4630 0.1080 341.56
0.5650 0.1040 340.57
0.5770 0.1960 336.16
0.5860 0.2950 332.30
0.6890 0.1930 334.01
0.6800 0.1030 338.70
0.7950 0.1470 334.09
0.8280 0.0740 338.68

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 94 (Gas)

Fixed Measured
Mole fraction of Ethanol (2) - Liquid Mole fraction of n-Hexane (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.1140 0.7730 332.11
0.1140 0.6640 334.13
0.1130 0.5630 336.14
0.1120 0.4670 338.16
0.1100 0.3750 340.22
0.1040 0.2800 342.88
0.1010 0.1920 345.56
0.0970 0.1050 348.85
0.1820 0.1030 346.28
0.1860 0.1840 343.12
0.1930 0.2710 340.31
0.1980 0.3610 337.82
0.2010 0.4630 335.51
0.1990 0.5710 333.37
0.1950 0.6860 331.45
0.2950 0.5870 331.36
0.2920 0.4880 333.27
0.2900 0.3890 335.39
0.2880 0.2950 337.74
0.2850 0.2000 340.63
0.2830 0.1090 344.05
0.3800 0.1020 342.88
0.3870 0.1900 339.33
0.3930 0.2840 336.29
0.3880 0.3960 333.65
0.3930 0.4970 331.51
0.4930 0.3990 331.72
0.4680 0.2820 335.08
0.4700 0.1940 337.95
0.4630 0.1080 341.56
0.5650 0.1040 340.57
0.5770 0.1960 336.16
0.5860 0.2950 332.30
0.6890 0.1930 334.01
0.6800 0.1030 338.70
0.7950 0.1470 334.09
0.8280 0.0740 338.68

Sources