Mixture of Diethyl carbonate + Acetic acid ethenyl ester

Datasets

1. Mole fraction (2)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (2)
4. c_sound,fluid - Speed of Sound, m/s (2)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Acetic acid ethenyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Mole fraction of Acetic acid ethenyl ester (2) - Gas
0.0000	0.0000
0.0480	0.1400
0.1350	0.3600
0.2130	0.5200
0.3010	0.6530
0.3530	0.7150
0.3770	0.7410
0.4020	0.7690
0.4500	0.8110
0.4760	0.8340
0.4970	0.8500
0.5240	0.8660
0.5600	0.8870
0.5940	0.9070
0.6620	0.9340
0.7370	0.9560
0.8170	0.9740
0.8500	0.9800
0.8850	0.9860
0.9530	0.9950
1.0000	1.0000

Mole fraction of Acetic acid ethenyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Mole fraction of Acetic acid ethenyl ester (2) - Gas
0.0000	0.0000
0.0480	0.1400
0.1350	0.3600
0.2130	0.5200
0.3010	0.6530
0.3530	0.7150
0.3770	0.7410
0.4020	0.7690
0.4500	0.8110
0.4760	0.8340
0.4970	0.8500
0.5240	0.8660
0.5600	0.8870
0.5940	0.9070
0.6620	0.9340
0.7370	0.9560
0.8170	0.9740
0.8500	0.9800
0.8850	0.9860
0.9530	0.9950
1.0000	1.0000

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3822
0.0430	1.3826
0.1050	1.3832
0.1700	1.3837
0.1930	1.384
0.2540	1.3846
0.2990	1.385
0.3530	1.3855
0.4070	1.386
0.4580	1.3865
0.5070	1.3871
0.5560	1.3876
0.5980	1.388
0.6500	1.3886
0.6970	1.3892
0.7440	1.3897
0.8030	1.3903
0.8500	1.3909
0.9010	1.3914
0.9460	1.392
1.0000	1.3925

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3822
0.0430	1.3826
0.1050	1.3832
0.1700	1.3837
0.1930	1.384
0.2540	1.3846
0.2990	1.385
0.3530	1.3855
0.4070	1.386
0.4580	1.3865
0.5070	1.3871
0.5560	1.3876
0.5980	1.388
0.6500	1.3886
0.6970	1.3892
0.7440	1.3897
0.8030	1.3903
0.8500	1.3909
0.9010	1.3914
0.9460	1.392
1.0000	1.3925

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	969.0
0.0430	967.68
0.1050	965.65
0.1700	963.45
0.1930	962.74
0.2540	960.55
0.2990	958.92
0.3530	956.87
0.4070	954.79
0.4580	952.74
0.5070	950.71
0.5560	948.6
0.5980	946.73
0.6500	944.3
0.6970	942.05
0.7440	939.73
0.8030	936.72
0.8500	934.22
0.9010	931.44
0.9460	928.87
1.0000	925.59

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	969.0
0.0430	967.68
0.1050	965.65
0.1700	963.45
0.1930	962.74
0.2540	960.55
0.2990	958.92
0.3530	956.87
0.4070	954.79
0.4580	952.74
0.5070	950.71
0.5560	948.6
0.5980	946.73
0.6500	944.3
0.6970	942.05
0.7440	939.73
0.8030	936.72
0.8500	934.22
0.9010	931.44
0.9460	928.87
1.0000	925.59

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1176.1
0.0430	1174.2
0.1050	1171.2
0.1700	1167.9
0.1930	1166.9
0.2540	1163.6
0.2990	1161.2
0.3530	1158.2
0.4070	1155.2
0.4580	1152.3
0.5070	1149.3
0.5560	1146.4
0.5980	1143.7
0.6500	1140.4
0.6970	1137.2
0.7440	1134.1
0.8030	1130.1
0.8500	1126.7
0.9010	1123.1
0.9460	1119.8
1.0000	1115.6

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1176.1
0.0430	1174.2
0.1050	1171.2
0.1700	1167.9
0.1930	1166.9
0.2540	1163.6
0.2990	1161.2
0.3530	1158.2
0.4070	1155.2
0.4580	1152.3
0.5070	1149.3
0.5560	1146.4
0.5980	1143.7
0.6500	1140.4
0.6970	1137.2
0.7440	1134.1
0.8030	1130.1
0.8500	1126.7
0.9010	1123.1
0.9460	1119.8
1.0000	1115.6

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	399.60
0.0480	395.50
0.1350	389.40
0.2130	383.60
0.3010	377.60
0.3530	374.30
0.3770	372.70
0.4020	370.70
0.4500	367.90
0.4760	365.90
0.4970	364.40
0.5240	363.10
0.5600	361.10
0.5940	359.00
0.6620	356.00
0.7370	353.00
0.8170	350.00
0.8500	349.20
0.8850	348.10
0.9530	347.20
1.0000	346.10

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid ethenyl ester (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	399.60
0.0480	395.50
0.1350	389.40
0.2130	383.60
0.3010	377.60
0.3530	374.30
0.3770	372.70
0.4020	370.70
0.4500	367.90
0.4760	365.90
0.4970	364.40
0.5240	363.10
0.5600	361.10
0.5940	359.00
0.6620	356.00
0.7370	353.00
0.8170	350.00
0.8500	349.20
0.8850	348.10
0.9530	347.20
1.0000	346.10

Sources

• Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems