Mixture of Carbonic acid, dimethyl ester + Benzene, 1,3-dimethyl-

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 Benzene, 1,3-dimethyl- (2) [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Mole fraction of Benzene, 1,3-dimethyl- (2) - Gas
0.0000	0.0000
0.0695	0.0229
0.1328	0.0439
0.1725	0.0571
0.1973	0.0642
0.3935	0.1425
0.5061	0.1853
0.5973	0.2386
0.7279	0.3487
0.8145	0.4618
0.8792	0.5869
0.9293	0.7064
1.0000	1.0000

Mole fraction of Benzene, 1,3-dimethyl- (2) [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Mole fraction of Benzene, 1,3-dimethyl- (2) - Gas
0.0000	0.0000
0.0695	0.0229
0.1328	0.0439
0.1725	0.0571
0.1973	0.0642
0.3935	0.1425
0.5061	0.1853
0.5973	0.2386
0.7279	0.3487
0.8145	0.4618
0.8792	0.5869
0.9293	0.7064
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
0.0502	0.1251
0.1006	0.2423
0.1510	0.3448
0.2014	0.4257
0.2517	0.4985
0.3004	0.5547
0.3503	0.6027
0.4014	0.6387
0.4506	0.6607
0.5007	0.6707
0.5515	0.6683
0.6004	0.6529
0.6522	0.6247
0.7018	0.5847
0.7517	0.5299
0.8017	0.4576
0.8517	0.3674
0.9015	0.2636
0.9509	0.1411

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
0.0503	0.0776
0.1007	0.2004
0.1511	0.3137
0.2016	0.3891
0.2519	0.4688
0.3005	0.5316
0.3505	0.5772
0.4015	0.6085
0.4505	0.6417
0.4998	0.6487
0.5506	0.6466
0.5995	0.6317
0.6521	0.6043
0.7018	0.5652
0.7517	0.5069
0.8017	0.4326
0.8516	0.3425
0.9014	0.2305
0.9509	0.1054

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
0.0502	0.1251
0.1006	0.2423
0.1510	0.3448
0.2014	0.4257
0.2517	0.4985
0.3004	0.5547
0.3503	0.6027
0.4014	0.6387
0.4506	0.6607
0.5007	0.6707
0.5515	0.6683
0.6004	0.6529
0.6522	0.6247
0.7018	0.5847
0.7517	0.5299
0.8017	0.4576
0.8517	0.3674
0.9015	0.2636
0.9509	0.1411

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
0.0503	0.0776
0.1007	0.2004
0.1511	0.3137
0.2016	0.3891
0.2519	0.4688
0.3005	0.5316
0.3505	0.5772
0.4015	0.6085
0.4505	0.6417
0.4998	0.6487
0.5506	0.6466
0.5995	0.6317
0.6521	0.6043
0.7018	0.5652
0.7517	0.5069
0.8017	0.4326
0.8516	0.3425
0.9014	0.2305
0.9509	0.1054

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3688
0.0467	1.3769
0.0871	1.3836
0.1737	1.3973
0.2042	1.4021
0.2593	1.4101
0.3033	1.4167
0.3719	1.4262
0.4455	1.4359
0.4709	1.439
0.5421	1.4481
0.6549	1.4612
0.7672	1.4738
0.8662	1.4839
0.9400	1.4913
1.0000	1.497

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3688
0.0467	1.3769
0.0871	1.3836
0.1737	1.3973
0.2042	1.4021
0.2593	1.4101
0.3033	1.4167
0.3719	1.4262
0.4455	1.4359
0.4709	1.439
0.5421	1.4481
0.6549	1.4612
0.7672	1.4738
0.8662	1.4839
0.9400	1.4913
1.0000	1.497

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	360.73
0.0695	362.20
0.1328	363.10
0.1725	363.66
0.1973	364.16
0.3935	369.96
0.5061	373.53
0.5973	377.03
0.7279	383.50
0.8145	389.23
0.8792	394.72
0.9293	399.19
1.0000	409.13

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	360.73
0.0695	362.20
0.1328	363.10
0.1725	363.66
0.1973	364.16
0.3935	369.96
0.5061	373.53
0.5973	377.03
0.7279	383.50
0.8145	389.23
0.8792	394.72
0.9293	399.19
1.0000	409.13

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