Mixture of n-Hexane + 1,2-Ethanediol + Water

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

1,2-Ethanediol

Name
1,2-Ethanediol
InChI
InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
InChI Key
LYCAIKOWRPUZTN-UHFFFAOYSA-N
Formula
C2H6O2
SMILES
OCCO
Mol. Weight (g/mol)
62.07
CAS
107-21-1

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Temperature, K x Mole fraction (8)

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 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2
283.10 0.9699 0.0150 0.0056 0.1718
283.10 0.8014 0.1471 0.0064 0.0321
283.10 0.7512 0.2370 0.0056 0.0193
283.10 0.6608 0.3286 0.0077 0.0124
283.10 0.5602 0.4290 0.0077 0.0089
283.10 0.2966 0.7002 0.0176 0.0029
283.10 0.2347 0.7646 0.0089 0.0022
293.10 0.9487 0.0504 0.0101 0.1502
293.10 0.8250 0.1713 0.0096 0.0387
293.10 0.7195 0.2781 0.0094 0.0192
293.10 0.6080 0.3915 0.0104 0.0131
293.10 0.4983 0.5008 0.0063 0.0083
293.10 0.4025 0.5919 0.0069 0.0052
293.10 0.3382 0.6614 0.0055 0.0041
303.10 0.9133 0.0821 0.0329 0.1233
303.10 0.7907 0.2033 0.0216 0.0416
303.10 0.6590 0.3301 0.0167 0.0243
303.10 0.5025 0.4926 0.0107 0.0129
303.10 0.3486 0.6500 0.0169 0.0066
303.10 0.2814 0.7165 0.0131 0.0048
303.10 0.1937 0.8032 0.0108 0.0029
303.10 0.1684 0.8314 0.0022 0.0026
313.10 0.7689 0.2245 0.0090 0.0702
313.10 0.6530 0.3415 0.0104 0.0512
313.10 0.5838 0.4108 0.0116 0.0298
313.10 0.4434 0.5539 0.0198 0.0173
313.10 0.2777 0.7205 0.0174 0.0089
313.10 0.1986 0.7888 0.0068 0.0062

Mole fraction of 1,2-Ethanediol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2
283.15 0.1500 8.7000e-06
283.15 0.3000 0.0000
283.15 0.5000 0.0000
283.15 0.6997 0.0000
283.15 0.8494 0.0000
303.15 0.1500 0.0000
303.15 0.3000 0.0000
303.15 0.4999 0.0001
303.15 0.6996 0.0001
303.15 0.8491 0.0001
333.15 0.1500 0.0001
333.15 0.3000 0.0001
333.15 0.4999 0.0002
333.15 0.6995 0.0003
333.15 0.8487 0.0003

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

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 1
283.15 0.1500 5.3100e-06
283.15 0.3000 0.0000
283.15 0.5000 0.0001
283.15 0.6997 0.0005
283.15 0.8494 0.0008
303.15 0.1500 0.0000
303.15 0.3000 0.0000
303.15 0.4999 0.0002
303.15 0.6996 0.0006
303.15 0.8491 0.0011
333.15 0.1500 0.0000
333.15 0.3000 0.0001
333.15 0.4999 0.0003
333.15 0.6995 0.0007
333.15 0.8487 0.0015

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2
283.15 0.1500 0.0003
283.15 0.3000 0.0002
283.15 0.5000 0.0002
283.15 0.6997 0.0001
283.15 0.8494 0.0001
303.15 0.1500 0.0007
303.15 0.3000 0.0006
303.15 0.4999 0.0005
303.15 0.6996 0.0004
303.15 0.8491 0.0002
333.15 0.1500 0.0011
333.15 0.3000 0.0009
333.15 0.4999 0.0007
333.15 0.6995 0.0006
333.15 0.8487 0.0004

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 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2
283.10 0.9699 0.0150 0.0056 0.1718
283.10 0.8014 0.1471 0.0064 0.0321
283.10 0.7512 0.2370 0.0056 0.0193
283.10 0.6608 0.3286 0.0077 0.0124
283.10 0.5602 0.4290 0.0077 0.0089
283.10 0.2966 0.7002 0.0176 0.0029
283.10 0.2347 0.7646 0.0089 0.0022
293.10 0.9487 0.0504 0.0101 0.1502
293.10 0.8250 0.1713 0.0096 0.0387
293.10 0.7195 0.2781 0.0094 0.0192
293.10 0.6080 0.3915 0.0104 0.0131
293.10 0.4983 0.5008 0.0063 0.0083
293.10 0.4025 0.5919 0.0069 0.0052
293.10 0.3382 0.6614 0.0055 0.0041
303.10 0.9133 0.0821 0.0329 0.1233
303.10 0.7907 0.2033 0.0216 0.0416
303.10 0.6590 0.3301 0.0167 0.0243
303.10 0.5025 0.4926 0.0107 0.0129
303.10 0.3486 0.6500 0.0169 0.0066
303.10 0.2814 0.7165 0.0131 0.0048
303.10 0.1937 0.8032 0.0108 0.0029
303.10 0.1684 0.8314 0.0022 0.0026
313.10 0.7689 0.2245 0.0090 0.0702
313.10 0.6530 0.3415 0.0104 0.0512
313.10 0.5838 0.4108 0.0116 0.0298
313.10 0.4434 0.5539 0.0198 0.0173
313.10 0.2777 0.7205 0.0174 0.0089
313.10 0.1986 0.7888 0.0068 0.0062

Mole fraction of 1,2-Ethanediol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2
283.15 0.1500 8.7000e-06
283.15 0.3000 0.0000
283.15 0.5000 0.0000
283.15 0.6997 0.0000
283.15 0.8494 0.0000
303.15 0.1500 0.0000
303.15 0.3000 0.0000
303.15 0.4999 0.0001
303.15 0.6996 0.0001
303.15 0.8491 0.0001
333.15 0.1500 0.0001
333.15 0.3000 0.0001
333.15 0.4999 0.0002
333.15 0.6995 0.0003
333.15 0.8487 0.0003

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

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of n-Hexane (1) - Liquid mixture 1
283.15 0.1500 5.3100e-06
283.15 0.3000 0.0000
283.15 0.5000 0.0001
283.15 0.6997 0.0005
283.15 0.8494 0.0008
303.15 0.1500 0.0000
303.15 0.3000 0.0000
303.15 0.4999 0.0002
303.15 0.6996 0.0006
303.15 0.8491 0.0011
333.15 0.1500 0.0000
333.15 0.3000 0.0001
333.15 0.4999 0.0003
333.15 0.6995 0.0007
333.15 0.8487 0.0015

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Fixed Measured
Temperature, K - Liquid mixture 2 Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1 Mole fraction of Water (3) - Liquid mixture 2
283.15 0.1500 0.0003
283.15 0.3000 0.0002
283.15 0.5000 0.0002
283.15 0.6997 0.0001
283.15 0.8494 0.0001
303.15 0.1500 0.0007
303.15 0.3000 0.0006
303.15 0.4999 0.0005
303.15 0.6996 0.0004
303.15 0.8491 0.0002
333.15 0.1500 0.0011
333.15 0.3000 0.0009
333.15 0.4999 0.0007
333.15 0.6995 0.0006
333.15 0.8487 0.0004

Sources