Mixture of Ethyl formate + 2-Propanol

Datasets

1. η - Viscosity, Pa*s
2. Excess molar enthalpy (molar enthalpy
3. ρ_l - Mass density, kg/m3

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	0.0024
293.15	0.0814	0.0018
293.15	0.1589	0.0013
293.15	0.2351	0.0011
293.15	0.3413	0.0008
293.15	0.4351	0.0007
293.15	0.5587	0.0006
293.15	0.6507	0.0005
293.15	0.7349	0.0005
293.15	0.8498	0.0004
293.15	0.9394	0.0004
293.15	1.0000	0.0004
298.15	0.0000	0.0021
298.15	0.0814	0.0015
298.15	0.1589	0.0012
298.15	0.2351	0.0009
298.15	0.3413	0.0008
298.15	0.4351	0.0006
298.15	0.5587	0.0005
298.15	0.6507	0.0005
298.15	0.7349	0.0005
298.15	0.8498	0.0004
298.15	0.9394	0.0004
298.15	1.0000	0.0004
303.15	0.0000	0.0018
303.15	0.0814	0.0014
303.15	0.1589	0.0011
303.15	0.2351	0.0009
303.15	0.3413	0.0007
303.15	0.4351	0.0006
303.15	0.5587	0.0005
303.15	0.6507	0.0005
303.15	0.7349	0.0004
303.15	0.8498	0.0004
303.15	0.9394	0.0004
303.15	1.0000	0.0004
308.15	0.0000	0.0016
308.15	0.0814	0.0012
308.15	0.1589	0.0009
308.15	0.2351	0.0008
308.15	0.3413	0.0006
308.15	0.4351	0.0006
308.15	0.5587	0.0005
308.15	0.6507	0.0004
308.15	0.7349	0.0004
308.15	0.8498	0.0004
308.15	0.9394	0.0004
308.15	1.0000	0.0003
313.15	0.0000	0.0014
313.15	0.0814	0.0010
313.15	0.1589	0.0008
313.15	0.2351	0.0007
313.15	0.3413	0.0006
313.15	0.4351	0.0005
313.15	0.5587	0.0004
313.15	0.6507	0.0004
313.15	0.7349	0.0004
313.15	0.8498	0.0004
313.15	0.9394	0.0003
313.15	1.0000	0.0003
318.15	0.0000	0.0012
318.15	0.0814	0.0009
318.15	0.1589	0.0008
318.15	0.2351	0.0006
318.15	0.3413	0.0005
318.15	0.4351	0.0005
318.15	0.5587	0.0004
318.15	0.6507	0.0004
318.15	0.7349	0.0004
318.15	0.8498	0.0003
318.15	0.9394	0.0003
318.15	1.0000	0.0003
323.15	0.0000	0.0010
323.15	0.0814	0.0008
323.15	0.1589	0.0007
323.15	0.2351	0.0006
323.15	0.3413	0.0005
323.15	0.4351	0.0004
323.15	0.5587	0.0004
323.15	0.6507	0.0004
323.15	0.7349	0.0003
323.15	0.8498	0.0003
323.15	0.9394	0.0003
323.15	1.0000	0.0003

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl formate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	5000.00	0.0498	0.3371
298.15	5000.00	0.0993	0.6619
298.15	5000.00	0.1485	0.9260
298.15	5000.00	0.2008	1.1529
298.15	5000.00	0.2493	1.3245
298.15	5000.00	0.3009	1.4641
298.15	5000.00	0.3488	1.5616
298.15	5000.00	0.3997	1.635
298.15	5000.00	0.4503	1.675
298.15	5000.00	0.5005	1.6869
298.15	5000.00	0.5504	1.6652
298.15	5000.00	0.5999	1.6276
298.15	5000.00	0.6492	1.5569
298.15	5000.00	0.7013	1.4374
298.15	5000.00	0.7498	1.2999
298.15	5000.00	0.8012	1.1171
298.15	5000.00	0.8997	0.6544
298.15	5000.00	0.9500	0.3587
298.15	10000.00	0.0497	0.3099
298.15	10000.00	0.0990	0.6379
298.15	10000.00	0.1516	0.9142
298.15	10000.00	0.2003	1.1323
298.15	10000.00	0.2487	1.3015
298.15	10000.00	0.3002	1.4435
298.15	10000.00	0.3514	1.5392
298.15	10000.00	0.3989	1.6029
298.15	10000.00	0.4495	1.644
298.15	10000.00	0.4997	1.6555
298.15	10000.00	0.5496	1.6437
298.15	10000.00	0.5991	1.6055
298.15	10000.00	0.6484	1.5379
298.15	10000.00	0.7006	1.4234
298.15	10000.00	0.7492	1.2986
298.15	10000.00	0.8006	1.1083
298.15	10000.00	0.8994	0.6550
298.15	10000.00	0.9499	0.3617
308.15	10000.00	0.0487	0.2137
308.15	10000.00	0.1000	0.5803
308.15	10000.00	0.1511	0.8840
308.15	10000.00	0.1988	1.116
308.15	10000.00	0.2492	1.3115
308.15	10000.00	0.2993	1.4676
308.15	10000.00	0.3490	1.5829
308.15	10000.00	0.4013	1.6663
308.15	10000.00	0.4504	1.7131
308.15	10000.00	0.4992	1.7276
308.15	10000.00	0.5505	1.7125
308.15	10000.00	0.5987	1.6704
308.15	10000.00	0.6996	1.476
308.15	10000.00	0.7496	1.3361
308.15	10000.00	0.7993	1.1638
308.15	10000.00	0.8513	0.9437
308.15	10000.00	0.9003	0.6831
308.15	10000.00	0.9490	0.3811

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	785.4
293.15	0.0814	795.4
293.15	0.1589	804.8
293.15	0.2351	814.0
293.15	0.3413	826.8
293.15	0.4351	838.3
293.15	0.5587	853.9
293.15	0.6507	865.7
293.15	0.7349	877.1
293.15	0.8498	893.5
293.15	0.9394	907.1
293.15	1.0000	916.6
298.15	0.0000	781.1
298.15	0.0814	790.7
298.15	0.1589	799.9
298.15	0.2351	808.8
298.15	0.3413	821.5
298.15	0.4351	832.8
298.15	0.5587	848.2
298.15	0.6507	859.9
298.15	0.7349	871.0
298.15	0.8498	887.2
298.15	0.9394	900.6
298.15	1.0000	910.1
303.15	0.0000	776.8
303.15	0.0814	786.1
303.15	0.1589	795.0
303.15	0.2351	803.8
303.15	0.3413	816.2
303.15	0.4351	827.4
303.15	0.5587	842.5
303.15	0.6507	854.0
303.15	0.7349	865.0
303.15	0.8498	880.8
303.15	0.9394	894.0
303.15	1.0000	903.6
308.15	0.0000	772.4
308.15	0.0814	781.4
308.15	0.1589	790.1
308.15	0.2351	798.8
308.15	0.3413	811.0
308.15	0.4351	822.0
308.15	0.5587	836.8
308.15	0.6507	848.0
308.15	0.7349	858.6
308.15	0.8498	874.1
308.15	0.9394	887.3
308.15	1.0000	897.1
313.15	0.0000	768.0
313.15	0.0814	776.6
313.15	0.1589	785.1
313.15	0.2351	793.6
313.15	0.3413	805.7
313.15	0.4351	816.5
313.15	0.5587	831.1
313.15	0.6507	842.1
313.15	0.7349	852.4
313.15	0.8498	867.6
313.15	0.9394	880.8
313.15	1.0000	890.5
318.15	0.0000	763.4
318.15	0.0814	771.8
318.15	0.1589	780.1
318.15	0.2351	788.3
318.15	0.3413	800.0
318.15	0.4351	810.5
318.15	0.5587	824.7
318.15	0.6507	835.4
318.15	0.7349	845.6
318.15	0.8498	860.4
318.15	0.9394	873.5
318.15	1.0000	883.0
323.15	0.0000	758.8
323.15	0.0814	766.7
323.15	0.1589	774.8
323.15	0.2351	782.8
323.15	0.3413	794.4
323.15	0.4351	804.8
323.15	0.5587	818.6
323.15	0.6507	829.2
323.15	0.7349	839.1
323.15	0.8498	853.8
323.15	0.9394	866.7
323.15	1.0000	876.0

Sources

• Excess molar enthalpies of ethylformate and (1-propanol, 2-propanol, 1-butanol, 2-butanol, and 1-pentanol) at T = (298.15 and 308.15) K and p = (5 and 10) MPa
• Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory

Note: These property values are available through the Cheméo API. A free account gives you an access key.