Mixture of Ethyl Acetate + Cyclohexane

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. Vapor Liquid Equilibrium at Constant Pressure
4. Vapor Liquid Equilibrium at Constant Temperature (2)

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0004
0.1042	0.0004
0.2074	0.0004
0.3097	0.0004
0.4111	0.0005
0.5115	0.0005
0.6110	0.0005
0.7095	0.0006
0.8072	0.0007
0.9040	0.0007
1.0000	0.0009

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0004
0.1042	0.0004
0.2074	0.0004
0.3097	0.0004
0.4111	0.0005
0.5115	0.0005
0.6110	0.0005
0.7095	0.0006
0.8072	0.0007
0.9040	0.0007
1.0000	0.0009

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	894.5
0.1042	877.0
0.2074	861.2
0.3097	847.0
0.4111	833.9
0.5115	822.1
0.6110	811.2
0.7095	801.2
0.8072	791.8
0.9040	782.7
1.0000	773.8

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	894.5
0.1042	877.0
0.2074	861.2
0.3097	847.0
0.4111	833.9
0.5115	822.1
0.6110	811.2
0.7095	801.2
0.8072	791.8
0.9040	782.7
1.0000	773.8

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Ethyl Acetate (1) - Liquid	y1[mol/mol] of Ethyl Acetate (1) - Vapour
350.65	0.0600	0.1400
348.85	0.1090	0.2230
346.95	0.1990	0.3220
346.15	0.2610	0.3670
345.25	0.3560	0.4320
344.85	0.4340	0.4800
344.85	0.4750	0.5030
344.75	0.5810	0.5630
344.95	0.6650	0.6160
345.55	0.7520	0.6830
346.45	0.8360	0.7590
347.35	0.8940	0.8270
348.35	0.9340	0.8840

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 293.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethyl Acetate (1) - Liquid	y1[mol/mol] of Ethyl Acetate (1) - Vapour
10.386	0.0000	0.0000
11.132	0.0250	0.0750
11.666	0.0500	0.1480
12.199	0.0750	0.1970
12.959	0.1440	0.2860
13.732	0.2180	0.3500
13.919	0.2740	0.3900
14.066	0.3470	0.4250
14.132	0.4060	0.4420
14.132	0.4940	0.4760
14.052	0.5750	0.5050
13.719	0.6900	0.5560
12.946	0.7870	0.6190
12.026	0.8870	0.7300
10.986	0.9480	0.8400
9.786	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Ethyl Acetate (1) - Liquid	y1[mol/mol] of Ethyl Acetate (1) - Vapour
47.169	0.0490	0.1290
51.7	0.1190	0.2350
54.01	0.1800	0.3100
54.919	0.2100	0.3290
55.439	0.2410	0.3520
57.09	0.3550	0.4250
57.85	0.4480	0.4680
58.01	0.5270	0.5210
57.81	0.5490	0.5280
57.641	0.6030	0.5630
57.199	0.6680	0.6010
56.161	0.7350	0.6440
55.459	0.7640	0.6720
53.46	0.8210	0.7220
49.9	0.9300	0.8690
48.569	0.9660	0.9240

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K