Mixture of Methane + Decane + Tetradecane

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. Vapor or sublimation pressure, kPa (2)

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Methane (1) - Liquid	Mole fraction of Decane (2) - Liquid	Viscosity, Pa*s - Liquid
294.40	0.0610	0.4700	0.0015
294.40	0.1490	0.4250	0.0013
294.50	0.1940	0.4030	0.0012
294.60	0.0590	0.7060	0.0011
294.60	0.1060	0.4470	0.0014
294.60	0.1510	0.2120	0.0015
294.70	0.1060	0.6710	0.0010
294.70	0.1890	0.2030	0.0014
294.70	0.2930	0.5300	0.0007
294.70	0.3290	0.5030	0.0007
294.80	0.0620	0.2350	0.0017
294.80	0.1470	0.6400	0.0010
294.90	0.1050	0.2240	0.0016
294.90	0.1920	0.6060	0.0009
294.90	0.2270	0.3860	0.0011
295.00	0.2280	0.5790	0.0009
295.20	0.2630	0.5530	0.0008
295.20	0.2940	0.3530	0.0010
295.20	0.3240	0.3380	0.0008
295.30	0.2310	0.1920	0.0014
295.30	0.2690	0.3660	0.0010
295.40	0.2670	0.1830	0.0013
295.80	0.3010	0.1750	0.0012
295.80	0.3270	0.1680	0.0011

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Methane (1) - Liquid	Mole fraction of Decane (2) - Liquid	Viscosity, Pa*s - Liquid
294.40	0.0610	0.4700	0.0015
294.40	0.1490	0.4250	0.0013
294.50	0.1940	0.4030	0.0012
294.60	0.0590	0.7060	0.0011
294.60	0.1060	0.4470	0.0014
294.60	0.1510	0.2120	0.0015
294.70	0.1060	0.6710	0.0010
294.70	0.1890	0.2030	0.0014
294.70	0.2930	0.5300	0.0007
294.70	0.3290	0.5030	0.0007
294.80	0.0620	0.2350	0.0017
294.80	0.1470	0.6400	0.0010
294.90	0.1050	0.2240	0.0016
294.90	0.1920	0.6060	0.0009
294.90	0.2270	0.3860	0.0011
295.00	0.2280	0.5790	0.0009
295.20	0.2630	0.5530	0.0008
295.20	0.2940	0.3530	0.0010
295.20	0.3240	0.3380	0.0008
295.30	0.2310	0.1920	0.0014
295.30	0.2690	0.3660	0.0010
295.40	0.2670	0.1830	0.0013
295.80	0.3010	0.1750	0.0012
295.80	0.3270	0.1680	0.0011

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Methane (1) - Liquid	Mole fraction of Decane (2) - Liquid	Mass density, kg/m3 - Liquid
294.40	0.0610	0.4700	741.0
294.40	0.1490	0.4250	731.0
294.50	0.1940	0.4030	726.0
294.60	0.0590	0.7060	730.0
294.60	0.1060	0.4470	736.0
294.60	0.1510	0.2120	738.0
294.70	0.1060	0.6710	725.0
294.70	0.1890	0.2030	733.0
294.70	0.2930	0.5300	702.0
294.70	0.3290	0.5030	698.0
294.80	0.0620	0.2350	746.0
294.80	0.1470	0.6400	721.0
294.90	0.1050	0.2240	742.0
294.90	0.1920	0.6060	717.0
294.90	0.2270	0.3860	721.0
295.00	0.2280	0.5790	712.0
295.20	0.2630	0.5530	707.0
295.20	0.2940	0.3530	712.0
295.20	0.3240	0.3380	707.0
295.30	0.2310	0.1920	729.0
295.30	0.2690	0.3660	716.0
295.40	0.2670	0.1830	724.0
295.80	0.3010	0.1750	720.0
295.80	0.3270	0.1680	716.0

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Methane (1) - Liquid	Mole fraction of Decane (2) - Liquid	Mass density, kg/m3 - Liquid
294.40	0.0610	0.4700	741.0
294.40	0.1490	0.4250	731.0
294.50	0.1940	0.4030	726.0
294.60	0.0590	0.7060	730.0
294.60	0.1060	0.4470	736.0
294.60	0.1510	0.2120	738.0
294.70	0.1060	0.6710	725.0
294.70	0.1890	0.2030	733.0
294.70	0.2930	0.5300	702.0
294.70	0.3290	0.5030	698.0
294.80	0.0620	0.2350	746.0
294.80	0.1470	0.6400	721.0
294.90	0.1050	0.2240	742.0
294.90	0.1920	0.6060	717.0
294.90	0.2270	0.3860	721.0
295.00	0.2280	0.5790	712.0
295.20	0.2630	0.5530	707.0
295.20	0.2940	0.3530	712.0
295.20	0.3240	0.3380	707.0
295.30	0.2310	0.1920	729.0
295.30	0.2690	0.3660	716.0
295.40	0.2670	0.1830	724.0
295.80	0.3010	0.1750	720.0
295.80	0.3270	0.1680	716.0

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Temperature, K - Gas	Mole fraction of Methane (1) - Gas	Mole fraction of Decane (2) - Gas	Vapor or sublimation pressure, kPa - Gas
294.40	0.0610	0.4700	1080.00
294.40	0.1490	0.4250	3010.00
294.50	0.1940	0.4030	4010.00
294.60	0.0590	0.7060	990.00
294.60	0.1060	0.4470	2020.00
294.60	0.1510	0.2120	3040.00
294.70	0.1060	0.6710	2010.00
294.70	0.1890	0.2030	4020.00
294.70	0.2930	0.5300	6940.00
294.70	0.3290	0.5030	8020.00
294.80	0.0620	0.2350	1090.00
294.80	0.1470	0.6400	2980.00
294.90	0.1050	0.2240	2030.00
294.90	0.1920	0.6060	4010.00
294.90	0.2270	0.3860	5000.00
295.00	0.2280	0.5790	5060.00
295.20	0.2630	0.5530	6000.00
295.20	0.2940	0.3530	6960.00
295.20	0.3240	0.3380	7990.00
295.30	0.2310	0.1920	4960.00
295.30	0.2690	0.3660	6010.00
295.40	0.2670	0.1830	6010.00
295.80	0.3010	0.1750	6990.00
295.80	0.3270	0.1680	8020.00

Vapor or sublimation pressure, kPa [ref]

Fixed			Measured
Temperature, K - Gas	Mole fraction of Methane (1) - Gas	Mole fraction of Decane (2) - Gas	Vapor or sublimation pressure, kPa - Gas
294.40	0.0610	0.4700	1080.00
294.40	0.1490	0.4250	3010.00
294.50	0.1940	0.4030	4010.00
294.60	0.0590	0.7060	990.00
294.60	0.1060	0.4470	2020.00
294.60	0.1510	0.2120	3040.00
294.70	0.1060	0.6710	2010.00
294.70	0.1890	0.2030	4020.00
294.70	0.2930	0.5300	6940.00
294.70	0.3290	0.5030	8020.00
294.80	0.0620	0.2350	1090.00
294.80	0.1470	0.6400	2980.00
294.90	0.1050	0.2240	2030.00
294.90	0.1920	0.6060	4010.00
294.90	0.2270	0.3860	5000.00
295.00	0.2280	0.5790	5060.00
295.20	0.2630	0.5530	6000.00
295.20	0.2940	0.3530	6960.00
295.20	0.3240	0.3380	7990.00
295.30	0.2310	0.1920	4960.00
295.30	0.2690	0.3660	6010.00
295.40	0.2670	0.1830	6010.00
295.80	0.3010	0.1750	6990.00
295.80	0.3270	0.1680	8020.00

Sources

• Experimental and thermodynamic modeling study on (vapor + liquid) equilibria and physical properties of ternary systems (methane + n-decane + n-tetradecane)