Mixture of n-Hexane + Acetone

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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

Acetone

Name
Acetone
InChI
InChI=1S/C3H6O/c1-3(2)4/h1-2H3
InChI Key
CSCPPACGZOOCGX-UHFFFAOYSA-N
Formula
C3H6O
SMILES
CC(C)=O
Mol. Weight (g/mol)
58.08
CAS
67-64-1
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Datasets

  1. n0 - Refractive index (Na D-line) (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Vapor Liquid Equilibrium at Constant Pressure
  4. Vapor Liquid Equilibrium at Constant Temperature (2)

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Acetone (2) - Liquid Refractive index (Na D-line) - Liquid
0.0504 1.3709
0.0994 1.3699
0.1511 1.3688
0.1999 1.3679
0.2497 1.3668
0.3006 1.366
0.3518 1.3651
0.4006 1.3643
0.4476 1.3635
0.4995 1.3627
0.5498 1.3618
0.5976 1.3611
0.6479 1.3603
0.6970 1.3595
0.7503 1.3587
0.7998 1.358
0.8499 1.3572
0.8979 1.3568
0.9507 1.3561

Refractive index (Na D-line) [ref]

Operational conditions:

Mole fraction of Acetone (2) - Liquid Refractive index (Na D-line) - Liquid
0.0504 1.3709
0.0994 1.3699
0.1511 1.3688
0.1999 1.3679
0.2497 1.3668
0.3006 1.366
0.3518 1.3651
0.4006 1.3643
0.4476 1.3635
0.4995 1.3627
0.5498 1.3618
0.5976 1.3611
0.6479 1.3603
0.6970 1.3595
0.7503 1.3587
0.7998 1.358
0.8499 1.3572
0.8979 1.3568
0.9507 1.3561

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Acetone (2) - Liquid Mass density, kg/m3 - Liquid
0.0504 657.2
0.0994 659.7
0.1511 662.9
0.1999 666.3
0.2497 670.1
0.3006 674.4
0.3518 679.0
0.4006 683.7
0.4476 688.7
0.4995 694.5
0.5498 700.7
0.5976 707.0
0.6479 714.1
0.6970 721.7
0.7503 730.5
0.7998 739.4
0.8499 749.1
0.8979 759.3
0.9507 771.7

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Acetone (2) - Liquid Mass density, kg/m3 - Liquid
0.0504 657.2
0.0994 659.7
0.1511 662.9
0.1999 666.3
0.2497 670.1
0.3006 674.4
0.3518 679.0
0.4006 683.7
0.4476 688.7
0.4995 694.5
0.5498 700.7
0.5976 707.0
0.6479 714.1
0.6970 721.7
0.7503 730.5
0.7998 739.4
0.8499 749.1
0.8979 759.3
0.9507 771.7

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetone (2) - Liquid y1[mol/mol] of Acetone (2) - Vapour
341.9 0.0000 0.0000
332.06 0.0942 0.3350
326.66 0.1986 0.4830
324.72 0.2989 0.5400
323.69 0.3983 0.5840
323.15 0.4995 0.6100
322.93 0.5999 0.6160
322.99 0.6999 0.6540
323.46 0.8007 0.7000
324.91 0.9015 0.7950
329.4 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (2) - Liquid y1[mol/mol] of Acetone (2) - Vapour
45.25 0.0000 0.0000
59.275 0.0651 0.2828
72.767 0.1592 0.4442
78.687 0.2549 0.5163
82.3 0.3478 0.5560
84.34 0.4429 0.5866
85.273 0.5210 0.6068
84.5 0.5907 0.6258
84.94 0.6202 0.6339
84.126 0.7168 0.6662
83.7 0.7923 0.7034
83.1 0.8022 0.7292
80.447 0.8692 0.7583
77.754 0.9288 0.8255
72.434 0.9658 0.9003
67.328 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 338.15 (VLE)

Fixed Measured
P [kPa] - VLE x1[mol/mol] of Acetone (2) - Liquid y1[mol/mol] of Acetone (2) - Vapour
152.774 0.2680 0.5280
160.133 0.3750 0.5700
165.04 0.4950 0.6130
168.16 0.6480 0.6750
167.506 0.6900 0.6900
167.64 0.7680 0.7400
155.707 0.9050 0.8400
147.521 0.9750 0.9400

Sources