Mixture of Ethyl formate + 2-Pentanol

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl formate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0040
293.15	0.0826	0.0028
293.15	0.1603	0.0022
293.15	0.2396	0.0017
293.15	0.3504	0.0013
293.15	0.4402	0.0011
293.15	0.5595	0.0009
293.15	0.6497	0.0008
293.15	0.7400	0.0006
293.15	0.8501	0.0005
293.15	0.9381	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0034
298.15	0.0826	0.0025
298.15	0.1603	0.0020
298.15	0.2396	0.0016
298.15	0.3504	0.0012
298.15	0.4402	0.0010
298.15	0.5595	0.0008
298.15	0.6497	0.0007
298.15	0.7400	0.0006
298.15	0.8501	0.0005
298.15	0.9381	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0029
303.15	0.0826	0.0022
303.15	0.1603	0.0017
303.15	0.2396	0.0014
303.15	0.3504	0.0011
303.15	0.4402	0.0009
303.15	0.5595	0.0008
303.15	0.6497	0.0007
303.15	0.7400	0.0006
303.15	0.8501	0.0005
303.15	0.9381	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0025
308.15	0.0826	0.0019
308.15	0.1603	0.0015
308.15	0.2396	0.0012
308.15	0.3504	0.0010
308.15	0.4402	0.0008
308.15	0.5595	0.0007
308.15	0.6497	0.0006
308.15	0.7400	0.0005
308.15	0.8501	0.0004
308.15	0.9381	0.0004
308.15	1.0000	0.0003
313.15	0.0000	0.0020
313.15	0.0826	0.0016
313.15	0.1603	0.0013
313.15	0.2396	0.0010
313.15	0.3504	0.0009
313.15	0.4402	0.0008
313.15	0.5595	0.0006
313.15	0.6497	0.0005
313.15	0.7400	0.0005
313.15	0.8501	0.0004
313.15	0.9381	0.0004
313.15	1.0000	0.0003
318.15	0.0000	0.0016
318.15	0.0826	0.0013
318.15	0.1603	0.0011
318.15	0.2396	0.0009
318.15	0.3504	0.0007
318.15	0.4402	0.0006
318.15	0.5595	0.0005
318.15	0.6497	0.0005
318.15	0.7400	0.0004
318.15	0.8501	0.0004
318.15	0.9381	0.0003
318.15	1.0000	0.0003
323.15	0.0000	0.0013
323.15	0.0826	0.0011
323.15	0.1603	0.0008
323.15	0.2396	0.0007
323.15	0.3504	0.0006
323.15	0.4402	0.0005
323.15	0.5595	0.0004
323.15	0.6497	0.0004
323.15	0.7400	0.0004
323.15	0.8501	0.0003
323.15	0.9381	0.0003
323.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl formate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0040
293.15	0.0826	0.0028
293.15	0.1603	0.0022
293.15	0.2396	0.0017
293.15	0.3504	0.0013
293.15	0.4402	0.0011
293.15	0.5595	0.0009
293.15	0.6497	0.0008
293.15	0.7400	0.0006
293.15	0.8501	0.0005
293.15	0.9381	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0034
298.15	0.0826	0.0025
298.15	0.1603	0.0020
298.15	0.2396	0.0016
298.15	0.3504	0.0012
298.15	0.4402	0.0010
298.15	0.5595	0.0008
298.15	0.6497	0.0007
298.15	0.7400	0.0006
298.15	0.8501	0.0005
298.15	0.9381	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0029
303.15	0.0826	0.0022
303.15	0.1603	0.0017
303.15	0.2396	0.0014
303.15	0.3504	0.0011
303.15	0.4402	0.0009
303.15	0.5595	0.0008
303.15	0.6497	0.0007
303.15	0.7400	0.0006
303.15	0.8501	0.0005
303.15	0.9381	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0025
308.15	0.0826	0.0019
308.15	0.1603	0.0015
308.15	0.2396	0.0012
308.15	0.3504	0.0010
308.15	0.4402	0.0008
308.15	0.5595	0.0007
308.15	0.6497	0.0006
308.15	0.7400	0.0005
308.15	0.8501	0.0004
308.15	0.9381	0.0004
308.15	1.0000	0.0003
313.15	0.0000	0.0020
313.15	0.0826	0.0016
313.15	0.1603	0.0013
313.15	0.2396	0.0010
313.15	0.3504	0.0009
313.15	0.4402	0.0008
313.15	0.5595	0.0006
313.15	0.6497	0.0005
313.15	0.7400	0.0005
313.15	0.8501	0.0004
313.15	0.9381	0.0004
313.15	1.0000	0.0003
318.15	0.0000	0.0016
318.15	0.0826	0.0013
318.15	0.1603	0.0011
318.15	0.2396	0.0009
318.15	0.3504	0.0007
318.15	0.4402	0.0006
318.15	0.5595	0.0005
318.15	0.6497	0.0005
318.15	0.7400	0.0004
318.15	0.8501	0.0004
318.15	0.9381	0.0003
318.15	1.0000	0.0003
323.15	0.0000	0.0013
323.15	0.0826	0.0011
323.15	0.1603	0.0008
323.15	0.2396	0.0007
323.15	0.3504	0.0006
323.15	0.4402	0.0005
323.15	0.5595	0.0004
323.15	0.6497	0.0004
323.15	0.7400	0.0004
323.15	0.8501	0.0003
323.15	0.9381	0.0003
323.15	1.0000	0.0003

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	809.3
293.15	0.0826	814.4
293.15	0.1603	819.6
293.15	0.2396	825.4
293.15	0.3504	834.5
293.15	0.4402	842.6
293.15	0.5595	854.7
293.15	0.6497	865.0
293.15	0.7400	876.4
293.15	0.8501	892.0
293.15	0.9381	906.0
293.15	1.0000	916.6
298.15	0.0000	805.3
298.15	0.0826	810.3
298.15	0.1603	815.4
298.15	0.2396	821.0
298.15	0.3504	829.7
298.15	0.4402	837.6
298.15	0.5595	849.4
298.15	0.6497	859.4
298.15	0.7400	870.4
298.15	0.8501	885.7
298.15	0.9381	899.4
298.15	1.0000	910.1
303.15	0.0000	801.2
303.15	0.0826	806.0
303.15	0.1603	811.0
303.15	0.2396	816.5
303.15	0.3504	825.0
303.15	0.4402	832.6
303.15	0.5595	844.0
303.15	0.6497	853.7
303.15	0.7400	864.6
303.15	0.8501	879.6
303.15	0.9381	893.0
303.15	1.0000	903.6
308.15	0.0000	797.0
308.15	0.0826	801.7
308.15	0.1603	806.5
308.15	0.2396	811.8
308.15	0.3504	820.0
308.15	0.4402	827.5
308.15	0.5595	838.7
308.15	0.6497	848.1
308.15	0.7400	858.7
308.15	0.8501	873.4
308.15	0.9381	886.7
308.15	1.0000	897.1
313.15	0.0000	792.7
313.15	0.0826	797.3
313.15	0.1603	802.0
313.15	0.2396	807.2
313.15	0.3504	815.2
313.15	0.4402	822.4
313.15	0.5595	833.2
313.15	0.6497	842.4
313.15	0.7400	852.9
313.15	0.8501	867.2
313.15	0.9381	880.2
313.15	1.0000	890.5
318.15	0.0000	788.4
318.15	0.0826	792.9
318.15	0.1603	797.4
318.15	0.2396	802.3
318.15	0.3504	809.9
318.15	0.4402	816.9
318.15	0.5595	827.3
318.15	0.6497	836.2
318.15	0.7400	846.2
318.15	0.8501	860.2
318.15	0.9381	872.8
318.15	1.0000	883.0
323.15	0.0000	784.0
323.15	0.0826	788.3
323.15	0.1603	792.6
323.15	0.2396	797.3
323.15	0.3504	804.7
323.15	0.4402	811.4
323.15	0.5595	821.5
323.15	0.6497	830.2
323.15	0.7400	839.9
323.15	0.8501	853.6
323.15	0.9381	866.0
323.15	1.0000	876.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	809.3
293.15	0.0826	814.4
293.15	0.1603	819.6
293.15	0.2396	825.4
293.15	0.3504	834.5
293.15	0.4402	842.6
293.15	0.5595	854.7
293.15	0.6497	865.0
293.15	0.7400	876.4
293.15	0.8501	892.0
293.15	0.9381	906.0
293.15	1.0000	916.6
298.15	0.0000	805.3
298.15	0.0826	810.3
298.15	0.1603	815.4
298.15	0.2396	821.0
298.15	0.3504	829.7
298.15	0.4402	837.6
298.15	0.5595	849.4
298.15	0.6497	859.4
298.15	0.7400	870.4
298.15	0.8501	885.7
298.15	0.9381	899.4
298.15	1.0000	910.1
303.15	0.0000	801.2
303.15	0.0826	806.0
303.15	0.1603	811.0
303.15	0.2396	816.5
303.15	0.3504	825.0
303.15	0.4402	832.6
303.15	0.5595	844.0
303.15	0.6497	853.7
303.15	0.7400	864.6
303.15	0.8501	879.6
303.15	0.9381	893.0
303.15	1.0000	903.6
308.15	0.0000	797.0
308.15	0.0826	801.7
308.15	0.1603	806.5
308.15	0.2396	811.8
308.15	0.3504	820.0
308.15	0.4402	827.5
308.15	0.5595	838.7
308.15	0.6497	848.1
308.15	0.7400	858.7
308.15	0.8501	873.4
308.15	0.9381	886.7
308.15	1.0000	897.1
313.15	0.0000	792.7
313.15	0.0826	797.3
313.15	0.1603	802.0
313.15	0.2396	807.2
313.15	0.3504	815.2
313.15	0.4402	822.4
313.15	0.5595	833.2
313.15	0.6497	842.4
313.15	0.7400	852.9
313.15	0.8501	867.2
313.15	0.9381	880.2
313.15	1.0000	890.5
318.15	0.0000	788.4
318.15	0.0826	792.9
318.15	0.1603	797.4
318.15	0.2396	802.3
318.15	0.3504	809.9
318.15	0.4402	816.9
318.15	0.5595	827.3
318.15	0.6497	836.2
318.15	0.7400	846.2
318.15	0.8501	860.2
318.15	0.9381	872.8
318.15	1.0000	883.0
323.15	0.0000	784.0
323.15	0.0826	788.3
323.15	0.1603	792.6
323.15	0.2396	797.3
323.15	0.3504	804.7
323.15	0.4402	811.4
323.15	0.5595	821.5
323.15	0.6497	830.2
323.15	0.7400	839.9
323.15	0.8501	853.6
323.15	0.9381	866.0
323.15	1.0000	876.0

Sources

• Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory