Mixture of n-Hexane + Carbonic acid, dimethyl ester

Datasets

1. η - Viscosity, Pa*s (4)
2. Excess molar enthalpy (molar enthalpy (2)
3. ρ_l - Mass density, kg/m3 (4)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0722	0.0003
293.15	0.1448	0.0003
293.15	0.2286	0.0003
293.15	0.3026	0.0003
293.15	0.4102	0.0004
293.15	0.5062	0.0004
293.15	0.6026	0.0004
293.15	0.7052	0.0005
293.15	0.7974	0.0005
293.15	0.9010	0.0006
293.15	0.9506	0.0006
293.15	1.0000	0.0006
298.15	0.0000	0.0003
298.15	0.0820	0.0003
298.15	0.1269	0.0003
298.15	0.2131	0.0003
298.15	0.3197	0.0003
298.15	0.3787	0.0003
298.15	0.4712	0.0004
298.15	0.5121	0.0004
298.15	0.6067	0.0004
298.15	0.6987	0.0004
298.15	0.8420	0.0005
298.15	0.9248	0.0005
298.15	0.9615	0.0006
298.15	1.0000	0.0006
303.15	0.0000	0.0003
303.15	0.0468	0.0003
303.15	0.0991	0.0003
303.15	0.1951	0.0003
303.15	0.2950	0.0003
303.15	0.3832	0.0003
303.15	0.4865	0.0003
303.15	0.5899	0.0004
303.15	0.6960	0.0004
303.15	0.7947	0.0004
303.15	0.8939	0.0005
303.15	0.9436	0.0005
303.15	1.0000	0.0005
313.15	0.0000	0.0003
313.15	0.0495	0.0003
313.15	0.1000	0.0003
313.15	0.2092	0.0003
313.15	0.3093	0.0003
313.15	0.4043	0.0003
313.15	0.4941	0.0003
313.15	0.6052	0.0003
313.15	0.7063	0.0004
313.15	0.8046	0.0004
313.15	0.9014	0.0005
313.15	0.9497	0.0005
313.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0961	0.0003
293.15	0.1930	0.0003
293.15	0.2909	0.0003
293.15	0.3894	0.0003
293.15	0.4890	0.0004
293.15	0.5893	0.0004
293.15	0.6906	0.0004
293.15	0.7928	0.0005
293.15	0.8960	0.0005
293.15	1.0000	0.0006
298.15	0.0000	0.0003
298.15	0.0961	0.0003
298.15	0.1930	0.0003
298.15	0.2909	0.0003
298.15	0.3894	0.0003
298.15	0.4890	0.0003
298.15	0.5893	0.0004
298.15	0.6906	0.0004
298.15	0.7928	0.0004
298.15	0.8960	0.0005
298.15	1.0000	0.0006
303.15	0.0000	0.0003
303.15	0.0961	0.0003
303.15	0.1930	0.0003
303.15	0.2909	0.0003
303.15	0.3894	0.0003
303.15	0.4890	0.0003
303.15	0.5893	0.0004
303.15	0.6906	0.0004
303.15	0.7928	0.0004
303.15	0.8960	0.0005
303.15	1.0000	0.0005
313.15	0.0000	0.0003
313.15	0.0961	0.0003
313.15	0.1930	0.0003
313.15	0.2909	0.0003
313.15	0.3894	0.0003
313.15	0.4890	0.0003
313.15	0.5893	0.0003
313.15	0.6906	0.0003
313.15	0.7928	0.0004
313.15	0.8960	0.0004
313.15	1.0000	0.0005
323.15	0.0000	0.0002
323.15	0.0961	0.0002
323.15	0.1930	0.0002
323.15	0.2909	0.0002
323.15	0.3894	0.0003
323.15	0.4890	0.0003
323.15	0.5893	0.0003
323.15	0.6906	0.0003
323.15	0.7928	0.0003
323.15	0.8960	0.0004
323.15	1.0000	0.0004
333.15	0.0000	0.0002
333.15	0.0961	0.0002
333.15	0.1930	0.0002
333.15	0.2909	0.0002
333.15	0.3894	0.0002
333.15	0.4890	0.0002
333.15	0.5893	0.0003
333.15	0.6906	0.0003
333.15	0.7928	0.0003
333.15	0.8960	0.0003
333.15	1.0000	0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0722	0.0003
293.15	0.1448	0.0003
293.15	0.2286	0.0003
293.15	0.3026	0.0003
293.15	0.4102	0.0004
293.15	0.5062	0.0004
293.15	0.6026	0.0004
293.15	0.7052	0.0005
293.15	0.7974	0.0005
293.15	0.9010	0.0006
293.15	0.9506	0.0006
293.15	1.0000	0.0006
298.15	0.0000	0.0003
298.15	0.0820	0.0003
298.15	0.1269	0.0003
298.15	0.2131	0.0003
298.15	0.3197	0.0003
298.15	0.3787	0.0003
298.15	0.4712	0.0004
298.15	0.5121	0.0004
298.15	0.6067	0.0004
298.15	0.6987	0.0004
298.15	0.8420	0.0005
298.15	0.9248	0.0005
298.15	0.9615	0.0006
298.15	1.0000	0.0006
303.15	0.0000	0.0003
303.15	0.0468	0.0003
303.15	0.0991	0.0003
303.15	0.1951	0.0003
303.15	0.2950	0.0003
303.15	0.3832	0.0003
303.15	0.4865	0.0003
303.15	0.5899	0.0004
303.15	0.6960	0.0004
303.15	0.7947	0.0004
303.15	0.8939	0.0005
303.15	0.9436	0.0005
303.15	1.0000	0.0005
313.15	0.0000	0.0003
313.15	0.0495	0.0003
313.15	0.1000	0.0003
313.15	0.2092	0.0003
313.15	0.3093	0.0003
313.15	0.4043	0.0003
313.15	0.4941	0.0003
313.15	0.6052	0.0003
313.15	0.7063	0.0004
313.15	0.8046	0.0004
313.15	0.9014	0.0005
313.15	0.9497	0.0005
313.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0961	0.0003
293.15	0.1930	0.0003
293.15	0.2909	0.0003
293.15	0.3894	0.0003
293.15	0.4890	0.0004
293.15	0.5893	0.0004
293.15	0.6906	0.0004
293.15	0.7928	0.0005
293.15	0.8960	0.0005
293.15	1.0000	0.0006
298.15	0.0000	0.0003
298.15	0.0961	0.0003
298.15	0.1930	0.0003
298.15	0.2909	0.0003
298.15	0.3894	0.0003
298.15	0.4890	0.0003
298.15	0.5893	0.0004
298.15	0.6906	0.0004
298.15	0.7928	0.0004
298.15	0.8960	0.0005
298.15	1.0000	0.0006
303.15	0.0000	0.0003
303.15	0.0961	0.0003
303.15	0.1930	0.0003
303.15	0.2909	0.0003
303.15	0.3894	0.0003
303.15	0.4890	0.0003
303.15	0.5893	0.0004
303.15	0.6906	0.0004
303.15	0.7928	0.0004
303.15	0.8960	0.0005
303.15	1.0000	0.0005
313.15	0.0000	0.0003
313.15	0.0961	0.0003
313.15	0.1930	0.0003
313.15	0.2909	0.0003
313.15	0.3894	0.0003
313.15	0.4890	0.0003
313.15	0.5893	0.0003
313.15	0.6906	0.0003
313.15	0.7928	0.0004
313.15	0.8960	0.0004
313.15	1.0000	0.0005
323.15	0.0000	0.0002
323.15	0.0961	0.0002
323.15	0.1930	0.0002
323.15	0.2909	0.0002
323.15	0.3894	0.0003
323.15	0.4890	0.0003
323.15	0.5893	0.0003
323.15	0.6906	0.0003
323.15	0.7928	0.0003
323.15	0.8960	0.0004
323.15	1.0000	0.0004
333.15	0.0000	0.0002
333.15	0.0961	0.0002
333.15	0.1930	0.0002
333.15	0.2909	0.0002
333.15	0.3894	0.0002
333.15	0.4890	0.0002
333.15	0.5893	0.0003
333.15	0.6906	0.0003
333.15	0.7928	0.0003
333.15	0.8960	0.0003
333.15	1.0000	0.0004

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

Operational conditions:

• Temperature, K = 318.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	0.0000
0.0880	0.7160
0.1762	1.223
0.2418	1.544
0.3259	1.808
0.4027	1.973
0.4703	2.049
0.5162	2.071
0.5554	2.06
0.6261	1.994
0.6776	1.904
0.7263	1.763
0.7728	1.594
0.8189	1.351
0.8660	1.096
0.9005	0.8520
0.9393	0.5450
0.9822	0.1970
1.0000	0.0000

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

Operational conditions:

• Temperature, K = 318.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	0.0000
0.0880	0.7160
0.1762	1.223
0.2418	1.544
0.3259	1.808
0.4027	1.973
0.4703	2.049
0.5162	2.071
0.5554	2.06
0.6261	1.994
0.6776	1.904
0.7263	1.763
0.7728	1.594
0.8189	1.351
0.8660	1.096
0.9005	0.8520
0.9393	0.5450
0.9822	0.1970
1.0000	0.0000

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	659.3
293.15	0.0722	677.3
293.15	0.1448	696.6
293.15	0.2286	720.8
293.15	0.3026	744.0
293.15	0.4102	780.8
293.15	0.5062	817.0
293.15	0.6026	857.1
293.15	0.7052	904.0
293.15	0.7974	950.5
293.15	0.9010	1008.3
293.15	0.9506	1038.5
293.15	1.0000	1070.0
298.15	0.0000	654.8
298.15	0.0820	674.9
298.15	0.1269	686.7
298.15	0.2131	710.9
298.15	0.3197	744.1
298.15	0.3787	764.0
298.15	0.4712	797.6
298.15	0.5121	813.4
298.15	0.6067	852.6
298.15	0.6987	894.5
298.15	0.8420	967.9
298.15	0.9248	1015.9
298.15	0.9615	1038.7
298.15	1.0000	1063.5
303.15	0.0000	650.4
303.15	0.0468	661.4
303.15	0.0991	674.5
303.15	0.1951	700.4
303.15	0.2950	730.4
303.15	0.3832	759.5
303.15	0.4865	797.1
303.15	0.5899	838.7
303.15	0.6960	886.3
303.15	0.7947	935.5
303.15	0.8939	990.5
303.15	0.9436	1020.3
303.15	1.0000	1056.5
313.15	0.0000	641.1
313.15	0.0495	652.7
313.15	0.1000	665.2
313.15	0.2092	694.5
313.15	0.3093	724.6
313.15	0.4043	756.1
313.15	0.4941	788.8
313.15	0.6052	833.6
313.15	0.7063	879.2
313.15	0.8046	928.6
313.15	0.9014	982.5
313.15	0.9497	1011.6
313.15	1.0000	1043.4
318.15	0.0000	636.4
318.15	0.0773	654.9
318.15	0.1163	664.6
318.15	0.1621	676.6
318.15	0.2689	706.8
318.15	0.3288	725.3
318.15	0.4097	752.4
318.15	0.4753	776.0
318.15	0.5256	795.2
318.15	0.5452	803.1
318.15	0.5879	820.6
318.15	0.6449	845.2
318.15	0.6976	869.3
318.15	0.7615	900.4
318.15	0.8039	922.2
318.15	0.8422	942.9
318.15	0.8808	964.3
318.15	0.9311	993.8
318.15	0.9657	1015.1
318.15	1.0000	1036.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	662.0
293.15	0.0961	685.68
293.15	0.1930	712.34
293.15	0.2909	741.99
293.15	0.3894	774.82
293.15	0.4890	811.38
293.15	0.5893	851.98
293.15	0.6906	897.34
293.15	0.7928	948.58
293.15	0.8960	1006.55
293.15	1.0000	1069.54
298.15	0.0000	657.44
298.15	0.0961	680.92
298.15	0.1930	707.38
298.15	0.2909	736.8
298.15	0.3894	769.42
298.15	0.4890	805.8
298.15	0.5893	846.19
298.15	0.6906	891.45
298.15	0.7928	942.39
298.15	0.8960	1000.17
298.15	1.0000	1062.95
303.15	0.0000	652.87
303.15	0.0961	676.14
303.15	0.1930	702.37
303.15	0.2909	731.62
303.15	0.3894	764.04
303.15	0.4890	800.21
303.15	0.5893	840.41
303.15	0.6906	885.48
303.15	0.7928	936.19
303.15	0.8960	993.78
303.15	1.0000	1056.35
313.15	0.0000	643.55
313.15	0.0961	666.41
313.15	0.1930	692.21
313.15	0.2909	721.04
313.15	0.3894	753.05
313.15	0.4890	788.82
313.15	0.5893	828.62
313.15	0.6906	873.34
313.15	0.7928	923.65
313.15	0.8960	980.84
313.15	1.0000	1043.01
323.15	0.0000	634.07
323.15	0.0961	656.55
323.15	0.1930	681.9
323.15	0.2909	710.27
323.15	0.3894	741.92
323.15	0.4890	777.28
323.15	0.5893	816.69
323.15	0.6906	861.07
323.15	0.7928	910.98
323.15	0.8960	967.8
323.15	1.0000	1029.59
333.15	0.0000	624.39
333.15	0.0961	646.44
333.15	0.1930	671.36
333.15	0.2909	699.25
333.15	0.3894	730.55
333.15	0.4890	765.5
333.15	0.5893	804.52
333.15	0.6906	848.53
333.15	0.7928	898.13
333.15	0.8960	954.54
333.15	1.0000	1016.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	659.3
293.15	0.0722	677.3
293.15	0.1448	696.6
293.15	0.2286	720.8
293.15	0.3026	744.0
293.15	0.4102	780.8
293.15	0.5062	817.0
293.15	0.6026	857.1
293.15	0.7052	904.0
293.15	0.7974	950.5
293.15	0.9010	1008.3
293.15	0.9506	1038.5
293.15	1.0000	1070.0
298.15	0.0000	654.8
298.15	0.0820	674.9
298.15	0.1269	686.7
298.15	0.2131	710.9
298.15	0.3197	744.1
298.15	0.3787	764.0
298.15	0.4712	797.6
298.15	0.5121	813.4
298.15	0.6067	852.6
298.15	0.6987	894.5
298.15	0.8420	967.9
298.15	0.9248	1015.9
298.15	0.9615	1038.7
298.15	1.0000	1063.5
303.15	0.0000	650.4
303.15	0.0468	661.4
303.15	0.0991	674.5
303.15	0.1951	700.4
303.15	0.2950	730.4
303.15	0.3832	759.5
303.15	0.4865	797.1
303.15	0.5899	838.7
303.15	0.6960	886.3
303.15	0.7947	935.5
303.15	0.8939	990.5
303.15	0.9436	1020.3
303.15	1.0000	1056.5
313.15	0.0000	641.1
313.15	0.0495	652.7
313.15	0.1000	665.2
313.15	0.2092	694.5
313.15	0.3093	724.6
313.15	0.4043	756.1
313.15	0.4941	788.8
313.15	0.6052	833.6
313.15	0.7063	879.2
313.15	0.8046	928.6
313.15	0.9014	982.5
313.15	0.9497	1011.6
313.15	1.0000	1043.4
318.15	0.0000	636.4
318.15	0.0773	654.9
318.15	0.1163	664.6
318.15	0.1621	676.6
318.15	0.2689	706.8
318.15	0.3288	725.3
318.15	0.4097	752.4
318.15	0.4753	776.0
318.15	0.5256	795.2
318.15	0.5452	803.1
318.15	0.5879	820.6
318.15	0.6449	845.2
318.15	0.6976	869.3
318.15	0.7615	900.4
318.15	0.8039	922.2
318.15	0.8422	942.9
318.15	0.8808	964.3
318.15	0.9311	993.8
318.15	0.9657	1015.1
318.15	1.0000	1036.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	662.0
293.15	0.0961	685.68
293.15	0.1930	712.34
293.15	0.2909	741.99
293.15	0.3894	774.82
293.15	0.4890	811.38
293.15	0.5893	851.98
293.15	0.6906	897.34
293.15	0.7928	948.58
293.15	0.8960	1006.55
293.15	1.0000	1069.54
298.15	0.0000	657.44
298.15	0.0961	680.92
298.15	0.1930	707.38
298.15	0.2909	736.8
298.15	0.3894	769.42
298.15	0.4890	805.8
298.15	0.5893	846.19
298.15	0.6906	891.45
298.15	0.7928	942.39
298.15	0.8960	1000.17
298.15	1.0000	1062.95
303.15	0.0000	652.87
303.15	0.0961	676.14
303.15	0.1930	702.37
303.15	0.2909	731.62
303.15	0.3894	764.04
303.15	0.4890	800.21
303.15	0.5893	840.41
303.15	0.6906	885.48
303.15	0.7928	936.19
303.15	0.8960	993.78
303.15	1.0000	1056.35
313.15	0.0000	643.55
313.15	0.0961	666.41
313.15	0.1930	692.21
313.15	0.2909	721.04
313.15	0.3894	753.05
313.15	0.4890	788.82
313.15	0.5893	828.62
313.15	0.6906	873.34
313.15	0.7928	923.65
313.15	0.8960	980.84
313.15	1.0000	1043.01
323.15	0.0000	634.07
323.15	0.0961	656.55
323.15	0.1930	681.9
323.15	0.2909	710.27
323.15	0.3894	741.92
323.15	0.4890	777.28
323.15	0.5893	816.69
323.15	0.6906	861.07
323.15	0.7928	910.98
323.15	0.8960	967.8
323.15	1.0000	1029.59
333.15	0.0000	624.39
333.15	0.0961	646.44
333.15	0.1930	671.36
333.15	0.2909	699.25
333.15	0.3894	730.55
333.15	0.4890	765.5
333.15	0.5893	804.52
333.15	0.6906	848.53
333.15	0.7928	898.13
333.15	0.8960	954.54
333.15	1.0000	1016.0

Sources

• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
• Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
• Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure