Mixture of n-Hexane + Isopropyl Alcohol

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

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0
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Datasets

  1. Mole fraction (2)
  2. Pc - Critical pressure, kPa (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. Tc - Critical temperature, K (2)
  5. Vapor Liquid Equilibrium at Constant Pressure (3)

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

Fixed Measured
Mole fraction of n-Hexane (1) - Liquid Temperature, K - Liquid Mole fraction of n-Hexane (1) - Gas
0.0000 483.15 0.0000
0.0000 493.15 0.0000
0.0000 503.15 0.0000
0.0220 503.15 0.0270
0.0290 483.15 0.0420
0.0400 493.15 0.0450
0.0480 503.15 0.0550
0.0680 493.15 0.0790
0.0780 483.15 0.0920
0.0870 503.15 0.0910
0.0990 503.15 0.0990
0.1160 493.15 0.1230
0.1650 483.15 0.1780
0.1660 493.15 0.1710
0.2180 493.15 0.2220
0.2340 483.15 0.2410
0.2870 493.15 0.2810
0.2950 483.15 0.3010
0.3280 483.15 0.3270
0.3500 493.15 0.3420
0.3790 493.15 0.3710
0.3870 483.15 0.3750
0.4180 493.15 0.4090
0.4270 493.15 0.4270
0.4660 483.15 0.4440
0.4990 483.15 0.4790
0.5580 493.15 0.5580
0.5650 483.15 0.5340
0.5660 493.15 0.5650
0.5900 493.15 0.5840
0.6240 483.15 0.5910
0.6850 493.15 0.6670
0.7480 483.15 0.7040
0.7720 493.15 0.7480
0.8020 483.15 0.7580
0.8370 493.15 0.8150
0.8970 493.15 0.8780
0.9040 483.15 0.8780
0.9060 503.15 0.9060
0.9120 503.15 0.9080
0.9280 503.15 0.9210
0.9350 493.15 0.9240
0.9470 503.15 0.9410
0.9730 503.15 0.9700
1.0000 483.15 1.0000
1.0000 493.15 1.0000
1.0000 503.15 1.0000

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

Fixed Measured
Mole fraction of n-Hexane (1) - Liquid Temperature, K - Liquid Mole fraction of n-Hexane (1) - Gas
0.0000 483.15 0.0000
0.0000 493.15 0.0000
0.0000 503.15 0.0000
0.0220 503.15 0.0270
0.0290 483.15 0.0420
0.0400 493.15 0.0450
0.0480 503.15 0.0550
0.0680 493.15 0.0790
0.0780 483.15 0.0920
0.0870 503.15 0.0910
0.0990 503.15 0.0990
0.1160 493.15 0.1230
0.1650 483.15 0.1780
0.1660 493.15 0.1710
0.2180 493.15 0.2220
0.2340 483.15 0.2410
0.2870 493.15 0.2810
0.2950 483.15 0.3010
0.3280 483.15 0.3270
0.3500 493.15 0.3420
0.3790 493.15 0.3710
0.3870 483.15 0.3750
0.4180 493.15 0.4090
0.4270 493.15 0.4270
0.4660 483.15 0.4440
0.4990 483.15 0.4790
0.5580 493.15 0.5580
0.5650 483.15 0.5340
0.5660 493.15 0.5650
0.5900 493.15 0.5840
0.6240 483.15 0.5910
0.6850 493.15 0.6670
0.7480 483.15 0.7040
0.7720 493.15 0.7480
0.8020 483.15 0.7580
0.8370 493.15 0.8150
0.8970 493.15 0.8780
0.9040 483.15 0.8780
0.9060 503.15 0.9060
0.9120 503.15 0.9080
0.9280 503.15 0.9210
0.9350 493.15 0.9240
0.9470 503.15 0.9410
0.9730 503.15 0.9700
1.0000 483.15 1.0000
1.0000 493.15 1.0000
1.0000 503.15 1.0000

Critical pressure, kPa [ref]

Mole fraction of n-Hexane (1) - Liquid Critical pressure, kPa - Liquid
0.0990 4546.00
0.4270 3921.00
0.5580 3726.00
0.9060 3214.00

Critical pressure, kPa [ref]

Mole fraction of n-Hexane (1) - Liquid Critical pressure, kPa - Liquid
0.0990 4546.00
0.4270 3921.00
0.5580 3726.00
0.9060 3214.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of n-Hexane (1) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 483.15 3081.00
0.0000 493.15 3677.00
0.0000 503.15 4362.00
0.0220 503.15 4420.00
0.0290 483.15 3141.00
0.0400 493.15 3760.00
0.0480 503.15 4470.00
0.0680 493.15 3810.00
0.0780 483.15 3222.00
0.0870 503.15 4546.00
0.0990 503.15 4546.00
0.1160 493.15 3878.00
0.1650 483.15 3321.00
0.1660 493.15 3932.00
0.2180 493.15 3961.00
0.2340 483.15 3359.00
0.2870 493.15 3985.00
0.2950 483.15 3375.00
0.3280 483.15 3376.00
0.3500 493.15 3978.00
0.3790 493.15 3958.00
0.3870 483.15 3354.00
0.4180 493.15 3932.00
0.4270 493.15 3921.00
0.4660 483.15 3306.00
0.4990 483.15 3274.00
0.5580 493.15 3726.00
0.5650 483.15 3194.00
0.5660 493.15 3712.00
0.5900 493.15 3671.00
0.6240 483.15 3104.00
0.6850 493.15 3468.00
0.7480 483.15 2862.00
0.7720 493.15 3239.00
0.8020 483.15 2743.00
0.8370 493.15 3050.00
0.8970 493.15 2847.00
0.9040 483.15 2431.00
0.9060 503.15 3214.00
0.9120 503.15 3200.00
0.9280 503.15 3143.00
0.9350 493.15 2680.00
0.9470 503.15 3062.00
0.9730 503.15 2945.00
1.0000 483.15 2109.00
1.0000 493.15 2453.00
1.0000 503.15 2838.00

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of n-Hexane (1) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 483.15 3081.00
0.0000 493.15 3677.00
0.0000 503.15 4362.00
0.0220 503.15 4420.00
0.0290 483.15 3141.00
0.0400 493.15 3760.00
0.0480 503.15 4470.00
0.0680 493.15 3810.00
0.0780 483.15 3222.00
0.0870 503.15 4546.00
0.0990 503.15 4546.00
0.1160 493.15 3878.00
0.1650 483.15 3321.00
0.1660 493.15 3932.00
0.2180 493.15 3961.00
0.2340 483.15 3359.00
0.2870 493.15 3985.00
0.2950 483.15 3375.00
0.3280 483.15 3376.00
0.3500 493.15 3978.00
0.3790 493.15 3958.00
0.3870 483.15 3354.00
0.4180 493.15 3932.00
0.4270 493.15 3921.00
0.4660 483.15 3306.00
0.4990 483.15 3274.00
0.5580 493.15 3726.00
0.5650 483.15 3194.00
0.5660 493.15 3712.00
0.5900 493.15 3671.00
0.6240 483.15 3104.00
0.6850 493.15 3468.00
0.7480 483.15 2862.00
0.7720 493.15 3239.00
0.8020 483.15 2743.00
0.8370 493.15 3050.00
0.8970 493.15 2847.00
0.9040 483.15 2431.00
0.9060 503.15 3214.00
0.9120 503.15 3200.00
0.9280 503.15 3143.00
0.9350 493.15 2680.00
0.9470 503.15 3062.00
0.9730 503.15 2945.00
1.0000 483.15 2109.00
1.0000 493.15 2453.00
1.0000 503.15 2838.00

Critical temperature, K [ref]

Mole fraction of n-Hexane (1) - Liquid Critical temperature, K - Liquid
0.0990 503.15
0.4270 493.15
0.5580 493.15
0.9060 503.15

Critical temperature, K [ref]

Mole fraction of n-Hexane (1) - Liquid Critical temperature, K - Liquid
0.0990 503.15
0.4270 493.15
0.5580 493.15
0.9060 503.15

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of n-Hexane (1) - Liquid y1[mol/mol] of n-Hexane (1) - Vapour
350.85 0.0325 0.1870
349.75 0.0420 0.2300
348.8 0.0525 0.2700
346.4 0.0825 0.3600
343.85 0.1175 0.4300
338.75 0.2420 0.5700
336.55 0.3725 0.6325
335.8 0.4575 0.6575
335.3 0.5500 0.6750
335.1 0.6175 0.7000
335.05 0.7220 0.7220
335.15 0.8100 0.7475
335.55 0.8600 0.7800
337.05 0.9500 0.8475

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 91.19 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of n-Hexane (1) - Liquid y1[mol/mol] of n-Hexane (1) - Vapour
345.85 0.0410 0.2600
339.35 0.1210 0.4850
335.15 0.2240 0.6100
333.35 0.2960 0.6550
332.35 0.4180 0.7060
332.25 0.5510 0.7250
332.15 0.6550 0.7300
332.25 0.7860 0.7550
333.45 0.9030 0.8110
336.25 0.9670 0.9000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of n-Hexane (1) - Liquid y1[mol/mol] of n-Hexane (1) - Vapour
350.85 0.0230 0.1360
343.2 0.0600 0.2570
341.4 0.1170 0.4240
337.85 0.2100 0.5580
337.25 0.2460 0.6000
337.05 0.2860 0.6370
335.4 0.3980 0.6720
335.35 0.4170 0.6720
335.05 0.4930 0.6910
334.7 0.5930 0.7060
334.75 0.6570 0.7200
334.7 0.6730 0.7250
334.75 0.7280 0.7270
334.95 0.8720 0.7580
335.65 0.9230 0.7990
337.05 0.9750 0.8560

Sources