Mixture of Carbonic acid, dimethyl ester + Ethylbenzene

Datasets

1. Mole fraction (2)
2. Excess molar enthalpy (molar enthalpy (4)
3. n₀ - Refractive index (Na D-line) (2)
4. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Ethylbenzene (2) [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Ethylbenzene (2) - Liquid	Mole fraction of Ethylbenzene (2) - Gas
0.0000	0.0000
0.0393	0.0219
0.0622	0.0330
0.1590	0.0693
0.2804	0.1104
0.3954	0.1475
0.4778	0.1782
0.6295	0.2524
0.7054	0.3081
0.8066	0.4176
0.8897	0.5730
0.9303	0.6839
1.0000	1.0000

Mole fraction of Ethylbenzene (2) [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Ethylbenzene (2) - Liquid	Mole fraction of Ethylbenzene (2) - Gas
0.0000	0.0000
0.0393	0.0219
0.0622	0.0330
0.1590	0.0693
0.2804	0.1104
0.3954	0.1475
0.4778	0.1782
0.6295	0.2524
0.7054	0.3081
0.8066	0.4176
0.8897	0.5730
0.9303	0.6839
1.0000	1.0000

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

Operational conditions:

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

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501	0.0899
0.1003	0.2048
0.1490	0.2674
0.2010	0.3548
0.2512	0.4344
0.2998	0.4993
0.3525	0.5570
0.4005	0.5997
0.4524	0.6289
0.5025	0.6418
0.5507	0.6416
0.6020	0.6297
0.6513	0.6054
0.7011	0.5651
0.7512	0.5131
0.8012	0.4455
0.8513	0.3620
0.9012	0.2607
0.9509	0.1403

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 10200 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501	0.1008
0.1004	0.2125
0.1491	0.2681
0.2011	0.3616
0.2514	0.4460
0.3000	0.5125
0.3528	0.5719
0.4009	0.6116
0.4528	0.6383
0.5028	0.6525
0.5510	0.6516
0.6023	0.6361
0.6517	0.6087
0.7014	0.5698
0.7514	0.5180
0.8014	0.4488
0.8514	0.3669
0.9013	0.2706
0.9508	0.1460

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

Operational conditions:

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

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501	0.0899
0.1003	0.2048
0.1490	0.2674
0.2010	0.3548
0.2512	0.4344
0.2998	0.4993
0.3525	0.5570
0.4005	0.5997
0.4524	0.6289
0.5025	0.6418
0.5507	0.6416
0.6020	0.6297
0.6513	0.6054
0.7011	0.5651
0.7512	0.5131
0.8012	0.4455
0.8513	0.3620
0.9012	0.2607
0.9509	0.1403

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 10200 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501	0.1008
0.1004	0.2125
0.1491	0.2681
0.2011	0.3616
0.2514	0.4460
0.3000	0.5125
0.3528	0.5719
0.4009	0.6116
0.4528	0.6383
0.5028	0.6525
0.5510	0.6516
0.6023	0.6361
0.6517	0.6087
0.7014	0.5698
0.7514	0.5180
0.8014	0.4488
0.8514	0.3669
0.9013	0.2706
0.9508	0.1460

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 93 (Liquid)
• Temperature, K = 293.15 (Liquid)

Mole fraction of Ethylbenzene (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3688
0.0462	1.3767
0.0890	1.3836
0.1753	1.397
0.2701	1.4109
0.3564	1.4232
0.4359	1.4335
0.4448	1.4352
0.4680	1.4382
0.5157	1.4441
0.5825	1.4527
0.6639	1.4617
0.7377	1.4702
0.8520	1.4815
0.8827	1.4847
0.9124	1.4873
0.9395	1.49
1.0000	1.4956

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 93 (Liquid)
• Temperature, K = 293.15 (Liquid)

Mole fraction of Ethylbenzene (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3688
0.0462	1.3767
0.0890	1.3836
0.1753	1.397
0.2701	1.4109
0.3564	1.4232
0.4359	1.4335
0.4448	1.4352
0.4680	1.4382
0.5157	1.4441
0.5825	1.4527
0.6639	1.4617
0.7377	1.4702
0.8520	1.4815
0.8827	1.4847
0.9124	1.4873
0.9395	1.49
1.0000	1.4956

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Ethylbenzene (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	360.73
0.0393	361.24
0.0622	361.55
0.1590	362.91
0.2804	364.85
0.3954	367.04
0.4778	368.97
0.6295	373.77
0.7054	377.14
0.8066	383.26
0.8897	390.65
0.9303	395.26
1.0000	406.23

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Ethylbenzene (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	360.73
0.0393	361.24
0.0622	361.55
0.1590	362.91
0.2804	364.85
0.3954	367.04
0.4778	368.97
0.6295	373.77
0.7054	377.14
0.8066	383.26
0.8897	390.65
0.9303	395.26
1.0000	406.23

Sources

• Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
• Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
• Excess Molar Enthalpies for Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene or Ethyl Benzoate at 298.15 K and 10.2 MPa