Mixture of Isopropyl Alcohol + Methane

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

Name: Methane
InChI: InChI=1S/CH4/h1H4
InChI Key: VNWKTOKETHGBQD-UHFFFAOYSA-N
Formula: CH4
SMILES: C
Mol. Weight (g/mol): 16.04
CAS: 74-82-8

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Datasets

Mole fraction (2)
η - Viscosity, Pa*s (2)
ρ_l - Mass density, kg/m3 (2)

Mole fraction of Methane (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Methane (2) - Liquid
302.80	1070.00	0.0190
302.80	2080.00	0.0370
302.80	3190.00	0.0550
302.80	4080.00	0.0690
302.80	5080.00	0.0850
302.80	6060.00	0.1000
323.10	980.00	0.0180
323.10	2020.00	0.0330
323.10	3080.00	0.0490
323.10	4080.00	0.0650
323.10	4980.00	0.0780
323.10	6040.00	0.0930

Mole fraction of Methane (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Methane (2) - Liquid
302.80	1070.00	0.0190
302.80	2080.00	0.0370
302.80	3190.00	0.0550
302.80	4080.00	0.0690
302.80	5080.00	0.0850
302.80	6060.00	0.1000
323.10	980.00	0.0180
323.10	2020.00	0.0330
323.10	3080.00	0.0490
323.10	4080.00	0.0650
323.10	4980.00	0.0780
323.10	6040.00	0.0930

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Methane (2) - Liquid	Viscosity, Pa*s - Liquid
302.80	1070.00	0.0190	0.0015
302.80	2080.00	0.0370	0.0014
302.80	3190.00	0.0550	0.0013
302.80	4080.00	0.0690	0.0013
302.80	5080.00	0.0850	0.0012
302.80	6060.00	0.1000	0.0011
323.10	980.00	0.0180	0.0009
323.10	2020.00	0.0330	0.0008
323.10	3080.00	0.0490	0.0008
323.10	4080.00	0.0650	0.0007
323.10	4980.00	0.0780	0.0007
323.10	6040.00	0.0930	0.0007

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Methane (2) - Liquid	Viscosity, Pa*s - Liquid
302.80	1070.00	0.0190	0.0015
302.80	2080.00	0.0370	0.0014
302.80	3190.00	0.0550	0.0013
302.80	4080.00	0.0690	0.0013
302.80	5080.00	0.0850	0.0012
302.80	6060.00	0.1000	0.0011
323.10	980.00	0.0180	0.0009
323.10	2020.00	0.0330	0.0008
323.10	3080.00	0.0490	0.0008
323.10	4080.00	0.0650	0.0007
323.10	4980.00	0.0780	0.0007
323.10	6040.00	0.0930	0.0007

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Methane (2) - Liquid	Mass density, kg/m3 - Liquid
302.80	1070.00	0.0190	771.2
302.80	2080.00	0.0370	767.2
302.80	3190.00	0.0550	761.2
302.80	4080.00	0.0690	756.5
302.80	5080.00	0.0850	753.3
302.80	6060.00	0.1000	748.9
323.10	980.00	0.0180	754.5
323.10	2020.00	0.0330	750.0
323.10	3080.00	0.0490	745.0
323.10	4080.00	0.0650	740.7
323.10	4980.00	0.0780	736.9
323.10	6040.00	0.0930	732.3

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Methane (2) - Liquid	Mass density, kg/m3 - Liquid
302.80	1070.00	0.0190	771.2
302.80	2080.00	0.0370	767.2
302.80	3190.00	0.0550	761.2
302.80	4080.00	0.0690	756.5
302.80	5080.00	0.0850	753.3
302.80	6060.00	0.1000	748.9
323.10	980.00	0.0180	754.5
323.10	2020.00	0.0330	750.0
323.10	3080.00	0.0490	745.0
323.10	4080.00	0.0650	740.7
323.10	4980.00	0.0780	736.9
323.10	6040.00	0.0930	732.3

Sources

Experimental and modeling investigations of solubility and saturated liquid densities and viscosities for binary systems (methane +, ethane +, and carbon dioxide + 2-propanol)