Mixture of Diethyl carbonate + n-Hexane

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_c - Critical pressure, kPa (2)
4. T_boil - Boiling temperature at pressure P, K (2)
5. T_c - Critical temperature, K (2)

Mole fraction of n-Hexane (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of n-Hexane (2) - Liquid	Mole fraction of n-Hexane (2) - Gas
0.0150	0.1290
0.0360	0.2640
0.0740	0.4410
0.1300	0.5960
0.1810	0.6810
0.2340	0.7460
0.2810	0.7810
0.3260	0.8100
0.3790	0.8330
0.4290	0.8570
0.4830	0.8680
0.5420	0.8850
0.5940	0.8980
0.6630	0.9150
0.7130	0.9280
0.7720	0.9350
0.8210	0.9460
0.8690	0.9570
0.9140	0.9690
0.9460	0.9790
0.9830	0.9930

Mole fraction of n-Hexane (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of n-Hexane (2) - Liquid	Mole fraction of n-Hexane (2) - Gas
0.0150	0.1290
0.0360	0.2640
0.0740	0.4410
0.1300	0.5960
0.1810	0.6810
0.2340	0.7460
0.2810	0.7810
0.3260	0.8100
0.3790	0.8330
0.4290	0.8570
0.4830	0.8680
0.5420	0.8850
0.5940	0.8980
0.6630	0.9150
0.7130	0.9280
0.7720	0.9350
0.8210	0.9460
0.8690	0.9570
0.9140	0.9690
0.9460	0.9790
0.9830	0.9930

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0576	0.0003
293.15	0.1106	0.0003
293.15	0.2219	0.0004
293.15	0.3358	0.0004
293.15	0.4303	0.0004
293.15	0.5384	0.0005
293.15	0.6357	0.0005
293.15	0.7334	0.0006
293.15	0.8246	0.0007
293.15	0.9171	0.0007
293.15	0.9589	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0003
298.15	0.0586	0.0003
298.15	0.1024	0.0003
298.15	0.2106	0.0003
298.15	0.3050	0.0004
298.15	0.3592	0.0004
298.15	0.4259	0.0004
298.15	0.5719	0.0005
298.15	0.7051	0.0005
298.15	0.7965	0.0006
298.15	0.8894	0.0007
298.15	0.9095	0.0007
298.15	0.9794	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0003
303.15	0.0583	0.0003
303.15	0.0941	0.0003
303.15	0.1925	0.0003
303.15	0.2897	0.0003
303.15	0.3927	0.0004
303.15	0.5087	0.0004
303.15	0.6072	0.0005
303.15	0.7059	0.0005
303.15	0.8002	0.0006
303.15	0.8947	0.0006
303.15	0.9532	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0003
313.15	0.0502	0.0003
313.15	0.1001	0.0003
313.15	0.2001	0.0003
313.15	0.3008	0.0003
313.15	0.4021	0.0003
313.15	0.4972	0.0004
313.15	0.5992	0.0004
313.15	0.7005	0.0005
313.15	0.8096	0.0005
313.15	0.8980	0.0006
313.15	0.9671	0.0006
313.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0576	0.0003
293.15	0.1106	0.0003
293.15	0.2219	0.0004
293.15	0.3358	0.0004
293.15	0.4303	0.0004
293.15	0.5384	0.0005
293.15	0.6357	0.0005
293.15	0.7334	0.0006
293.15	0.8246	0.0007
293.15	0.9171	0.0007
293.15	0.9589	0.0008
293.15	1.0000	0.0008
298.15	0.0000	0.0003
298.15	0.0586	0.0003
298.15	0.1024	0.0003
298.15	0.2106	0.0003
298.15	0.3050	0.0004
298.15	0.3592	0.0004
298.15	0.4259	0.0004
298.15	0.5719	0.0005
298.15	0.7051	0.0005
298.15	0.7965	0.0006
298.15	0.8894	0.0007
298.15	0.9095	0.0007
298.15	0.9794	0.0007
298.15	1.0000	0.0007
303.15	0.0000	0.0003
303.15	0.0583	0.0003
303.15	0.0941	0.0003
303.15	0.1925	0.0003
303.15	0.2897	0.0003
303.15	0.3927	0.0004
303.15	0.5087	0.0004
303.15	0.6072	0.0005
303.15	0.7059	0.0005
303.15	0.8002	0.0006
303.15	0.8947	0.0006
303.15	0.9532	0.0007
303.15	1.0000	0.0007
313.15	0.0000	0.0003
313.15	0.0502	0.0003
313.15	0.1001	0.0003
313.15	0.2001	0.0003
313.15	0.3008	0.0003
313.15	0.4021	0.0003
313.15	0.4972	0.0004
313.15	0.5992	0.0004
313.15	0.7005	0.0005
313.15	0.8096	0.0005
313.15	0.8980	0.0006
313.15	0.9671	0.0006
313.15	1.0000	0.0006

Critical pressure, kPa [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical pressure, kPa - Liquid
0.0750	3058.00
0.1542	3094.00
0.2382	3127.00
0.3272	3186.00
0.4218	3227.00
0.5225	3272.00
0.6299	3306.00
0.7448	3337.00
0.8678	3351.00

Critical pressure, kPa [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical pressure, kPa - Liquid
0.0750	3058.00
0.1542	3094.00
0.2382	3127.00
0.3272	3186.00
0.4218	3227.00
0.5225	3272.00
0.6299	3306.00
0.7448	3337.00
0.8678	3351.00

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of n-Hexane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0150	394.53
0.0360	389.82
0.0740	382.53
0.1300	373.85
0.1810	368.83
0.2340	364.08
0.2810	360.94
0.3260	358.40
0.3790	356.03
0.4290	354.17
0.4830	352.30
0.5420	350.65
0.5940	349.42
0.6630	347.87
0.7130	346.86
0.7720	345.75
0.8210	344.82
0.8690	343.88
0.9140	343.05
0.9460	342.40
0.9830	341.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of n-Hexane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0150	394.53
0.0360	389.82
0.0740	382.53
0.1300	373.85
0.1810	368.83
0.2340	364.08
0.2810	360.94
0.3260	358.40
0.3790	356.03
0.4290	354.17
0.4830	352.30
0.5420	350.65
0.5940	349.42
0.6630	347.87
0.7130	346.86
0.7720	345.75
0.8210	344.82
0.8690	343.88
0.9140	343.05
0.9460	342.40
0.9830	341.65

Critical temperature, K [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical temperature, K - Liquid
0.0750	510.10
0.1542	514.80
0.2382	520.80
0.3272	526.50
0.4218	532.30
0.5225	540.50
0.6299	549.20
0.7448	559.10
0.8678	568.60

Critical temperature, K [ref]

Mole fraction of Diethyl carbonate (1) - Liquid	Critical temperature, K - Liquid
0.0750	510.10
0.1542	514.80
0.2382	520.80
0.3272	526.50
0.4218	532.30
0.5225	540.50
0.6299	549.20
0.7448	559.10
0.8678	568.60

Sources

• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters