Mixture of p-Xylene + Carbonic acid, dimethyl ester

Datasets

1. Mole fraction (4)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
3. Excess molar enthalpy (molar enthalpy (4)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (2)
6. γ - Surface tension liquid-gas, N/m (2)
7. T_boil - Boiling temperature at pressure P, K (4)

Mole fraction of Carbonic acid, dimethyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Gas
1.0000	1.0000
0.8276	0.9399
0.7037	0.8899
0.6075	0.8517
0.4878	0.7909
0.4007	0.7355
0.3192	0.6730
0.2637	0.6160
0.2102	0.5532
0.1608	0.4728
0.1197	0.3880
0.0897	0.3157
0.0675	0.2542
0.0429	0.1831
0.0240	0.1129
0.0000	0.0000

Mole fraction of p-Xylene (1) [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of p-Xylene (1) - Liquid	Mole fraction of p-Xylene (1) - Gas
0.0000	0.0000
0.0551	0.0284
0.1334	0.0609
0.2270	0.0852
0.3045	0.1089
0.3575	0.1236
0.4678	0.1598
0.5688	0.1857
0.7372	0.2935
0.8416	0.4386
0.9369	0.6856
0.9749	0.8466
1.0000	1.0000

Mole fraction of Carbonic acid, dimethyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Gas
1.0000	1.0000
0.8276	0.9399
0.7037	0.8899
0.6075	0.8517
0.4878	0.7909
0.4007	0.7355
0.3192	0.6730
0.2637	0.6160
0.2102	0.5532
0.1608	0.4728
0.1197	0.3880
0.0897	0.3157
0.0675	0.2542
0.0429	0.1831
0.0240	0.1129
0.0000	0.0000

Mole fraction of p-Xylene (1) [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of p-Xylene (1) - Liquid	Mole fraction of p-Xylene (1) - Gas
0.0000	0.0000
0.0551	0.0284
0.1334	0.0609
0.2270	0.0852
0.3045	0.1089
0.3575	0.1236
0.4678	0.1598
0.5688	0.1857
0.7372	0.2935
0.8416	0.4386
0.9369	0.6856
0.9749	0.8466
1.0000	1.0000

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
288.15	0.0000	178.86
288.15	0.0452	178.07
288.15	0.0969	177.32
288.15	0.2003	175.72
288.15	0.3136	173.97
288.15	0.4125	172.39
288.15	0.4946	171.06
288.15	0.5368	170.43
288.15	0.6528	168.55
288.15	0.8445	165.60
288.15	0.9000	164.89
288.15	1.0000	163.61
298.15	0.0000	182.56
298.15	0.0452	181.79
298.15	0.0969	180.82
298.15	0.2003	178.96
298.15	0.3136	176.99
298.15	0.4125	175.09
298.15	0.4946	173.56
298.15	0.5368	172.79
298.15	0.6528	170.61
298.15	0.8445	167.14
298.15	0.9000	166.25
298.15	1.0000	164.65
308.15	0.0000	186.15
308.15	0.0452	185.28
308.15	0.0969	184.22
308.15	0.2003	182.14
308.15	0.3136	179.84
308.15	0.4125	177.74
308.15	0.4946	176.04
308.15	0.5368	175.13
308.15	0.6528	172.04
308.15	0.8445	168.84
308.15	0.9000	167.79
308.15	1.0000	165.92

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
288.15	0.0000	178.86
288.15	0.0452	178.07
288.15	0.0969	177.32
288.15	0.2003	175.72
288.15	0.3136	173.97
288.15	0.4125	172.39
288.15	0.4946	171.06
288.15	0.5368	170.43
288.15	0.6528	168.55
288.15	0.8445	165.60
288.15	0.9000	164.89
288.15	1.0000	163.61
298.15	0.0000	182.56
298.15	0.0452	181.79
298.15	0.0969	180.82
298.15	0.2003	178.96
298.15	0.3136	176.99
298.15	0.4125	175.09
298.15	0.4946	173.56
298.15	0.5368	172.79
298.15	0.6528	170.61
298.15	0.8445	167.14
298.15	0.9000	166.25
298.15	1.0000	164.65
308.15	0.0000	186.15
308.15	0.0452	185.28
308.15	0.0969	184.22
308.15	0.2003	182.14
308.15	0.3136	179.84
308.15	0.4125	177.74
308.15	0.4946	176.04
308.15	0.5368	175.13
308.15	0.6528	172.04
308.15	0.8445	168.84
308.15	0.9000	167.79
308.15	1.0000	165.92

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 (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0504	0.1233
0.1010	0.2271
0.1515	0.3502
0.2020	0.4284
0.2529	0.4991
0.3012	0.5552
0.3512	0.6066
0.4022	0.6419
0.4515	0.6633
0.5016	0.6740
0.5524	0.6702
0.6013	0.6517
0.6507	0.6227
0.7004	0.5812
0.7503	0.5231
0.8003	0.4558
0.8502	0.3679
0.9018	0.2598
0.9511	0.1381

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 (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0504	0.0668
0.1026	0.1883
0.1515	0.2930
0.2020	0.3560
0.2524	0.4402
0.3011	0.4981
0.3511	0.5725
0.4022	0.6134
0.4514	0.6357
0.5016	0.6402
0.5524	0.6377
0.6013	0.6207
0.6507	0.5976
0.7004	0.5521
0.7503	0.4891
0.8002	0.4324
0.8502	0.3468
0.9017	0.2350
0.9511	0.1074

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 (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0504	0.1233
0.1010	0.2271
0.1515	0.3502
0.2020	0.4284
0.2529	0.4991
0.3012	0.5552
0.3512	0.6066
0.4022	0.6419
0.4515	0.6633
0.5016	0.6740
0.5524	0.6702
0.6013	0.6517
0.6507	0.6227
0.7004	0.5812
0.7503	0.5231
0.8003	0.4558
0.8502	0.3679
0.9018	0.2598
0.9511	0.1381

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 (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0504	0.0668
0.1026	0.1883
0.1515	0.2930
0.2020	0.3560
0.2524	0.4402
0.3011	0.4981
0.3511	0.5725
0.4022	0.6134
0.4514	0.6357
0.5016	0.6402
0.5524	0.6377
0.6013	0.6207
0.6507	0.5976
0.7004	0.5521
0.7503	0.4891
0.8002	0.4324
0.8502	0.3468
0.9017	0.2350
0.9511	0.1074

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of p-Xylene (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3687
0.0368	1.3752
0.0866	1.3835
0.1570	1.3946
0.2639	1.4106
0.3598	1.4241
0.4244	1.4326
0.5293	1.4457
0.6397	1.4586
0.7655	1.4724
0.8832	1.4848
0.9380	1.4898
1.0000	1.4956

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of p-Xylene (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3687
0.0368	1.3752
0.0866	1.3835
0.1570	1.3946
0.2639	1.4106
0.3598	1.4241
0.4244	1.4326
0.5293	1.4457
0.6397	1.4586
0.7655	1.4724
0.8832	1.4848
0.9380	1.4898
1.0000	1.4956

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	0.0432	871.8
288.15	100.00	0.1950	894.2
288.15	100.00	0.3968	924.2
288.15	100.00	0.4933	944.9
288.15	100.00	0.5296	953.3
288.15	100.00	0.5993	968.4
288.15	100.00	0.7034	992.3
288.15	100.00	0.8023	1010.6
288.15	100.00	0.8921	1038.1
288.15	100.00	0.9478	1052.9
288.15	5000.00	0.0432	875.5
288.15	5000.00	0.1950	897.8
288.15	5000.00	0.3968	931.9
288.15	5000.00	0.4933	950.4
288.15	5000.00	0.5296	957.3
288.15	5000.00	0.5993	972.4
288.15	5000.00	0.7034	996.2
288.15	5000.00	0.8023	1014.9
288.15	5000.00	0.8921	1042.5
288.15	5000.00	0.9478	1057.2
288.15	10000.00	0.0432	879.1
288.15	10000.00	0.1950	901.3
288.15	10000.00	0.3968	935.7
288.15	10000.00	0.4933	954.1
288.15	10000.00	0.5296	961.2
288.15	10000.00	0.5993	976.3
288.15	10000.00	0.7034	1000.3
288.15	10000.00	0.8023	1019.0
288.15	10000.00	0.8921	1046.6
288.15	10000.00	0.9478	1061.4
288.15	20000.00	0.0432	885.4
288.15	20000.00	0.1950	907.8
288.15	20000.00	0.3968	942.5
288.15	20000.00	0.4933	961.4
288.15	20000.00	0.5296	968.3
288.15	20000.00	0.5993	983.7
288.15	20000.00	0.7034	1007.8
288.15	20000.00	0.8023	1026.8
288.15	20000.00	0.8921	1054.5
288.15	20000.00	0.9478	1069.4
288.15	30000.00	0.0432	891.3
288.15	30000.00	0.1950	914.0
288.15	30000.00	0.3968	949.0
288.15	30000.00	0.4933	967.9
288.15	30000.00	0.5296	974.9
288.15	30000.00	0.5993	990.5
288.15	30000.00	0.7034	1014.7
288.15	30000.00	0.8023	1033.9
288.15	30000.00	0.8921	1061.5
288.15	30000.00	0.9478	1076.7
288.15	40000.00	0.0432	897.1
288.15	40000.00	0.1950	920.1
288.15	40000.00	0.3968	955.3
288.15	40000.00	0.4933	974.3
288.15	40000.00	0.5296	980.9
288.15	40000.00	0.5993	997.1
288.15	40000.00	0.7034	1021.4
288.15	40000.00	0.8023	1040.7
288.15	40000.00	0.8921	1068.7
288.15	40000.00	0.9478	1083.8
298.15	100.00	0.0432	863.0
298.15	100.00	0.1950	884.5
298.15	100.00	0.3968	917.8
298.15	100.00	0.4933	935.8
298.15	100.00	0.5296	942.5
298.15	100.00	0.5993	957.3
298.15	100.00	0.7034	980.5
298.15	100.00	0.8023	998.4
298.15	100.00	0.8921	1025.5
298.15	100.00	0.9478	1040.0
298.15	5000.00	0.0432	867.3
298.15	5000.00	0.1950	888.3
298.15	5000.00	0.3968	922.5
298.15	5000.00	0.4933	940.6
298.15	5000.00	0.5296	947.1
298.15	5000.00	0.5993	962.0
298.15	5000.00	0.7034	985.4
298.15	5000.00	0.8023	1003.4
298.15	5000.00	0.8921	1030.6
298.15	5000.00	0.9478	1044.9
298.15	10000.00	0.0432	870.4
298.15	10000.00	0.1950	892.1
298.15	10000.00	0.3968	925.8
298.15	10000.00	0.4933	944.0
298.15	10000.00	0.5296	950.7
298.15	10000.00	0.5993	965.7
298.15	10000.00	0.7034	989.1
298.15	10000.00	0.8023	1007.3
298.15	10000.00	0.8921	1034.7
298.15	10000.00	0.9478	1049.0
298.15	20000.00	0.0432	877.1
298.15	20000.00	0.1950	899.2
298.15	20000.00	0.3968	933.2
298.15	20000.00	0.4933	951.6
298.15	20000.00	0.5296	958.2
298.15	20000.00	0.5993	973.4
298.15	20000.00	0.7034	997.0
298.15	20000.00	0.8023	1015.5
298.15	20000.00	0.8921	1042.9
298.15	20000.00	0.9478	1057.5
298.15	30000.00	0.0432	883.4
298.15	30000.00	0.1950	905.5
298.15	30000.00	0.3968	939.9
298.15	30000.00	0.4933	958.7
298.15	30000.00	0.5296	965.4
298.15	30000.00	0.5993	980.5
298.15	30000.00	0.7034	1004.4
298.15	30000.00	0.8023	1022.7
298.15	30000.00	0.8921	1050.6
298.15	30000.00	0.9478	1065.0
298.15	40000.00	0.0432	889.1
298.15	40000.00	0.1950	911.7
298.15	40000.00	0.3968	946.5
298.15	40000.00	0.4933	965.1
298.15	40000.00	0.5296	972.0
298.15	40000.00	0.5993	987.3
298.15	40000.00	0.7034	1011.2
298.15	40000.00	0.8023	1030.1
298.15	40000.00	0.8921	1057.9
298.15	40000.00	0.9478	1072.7
308.15	100.00	0.0432	854.3
308.15	100.00	0.1950	875.2
308.15	100.00	0.3968	907.6
308.15	100.00	0.4933	925.2
308.15	100.00	0.5296	931.7
308.15	100.00	0.5993	946.3
308.15	100.00	0.7034	969.0
308.15	100.00	0.8023	986.4
308.15	100.00	0.8921	1013.1
308.15	100.00	0.9478	1027.2
308.15	5000.00	0.0432	858.1
308.15	5000.00	0.1950	879.3
308.15	5000.00	0.3968	912.1
308.15	5000.00	0.4933	929.7
308.15	5000.00	0.5296	936.2
308.15	5000.00	0.5993	950.8
308.15	5000.00	0.7034	973.7
308.15	5000.00	0.8023	991.0
308.15	5000.00	0.8921	1018.0
308.15	5000.00	0.9478	1032.1
308.15	10000.00	0.0432	862.0
308.15	10000.00	0.1950	883.3
308.15	10000.00	0.3968	916.2
308.15	10000.00	0.4933	934.1
308.15	10000.00	0.5296	940.4
308.15	10000.00	0.5993	955.2
308.15	10000.00	0.7034	978.2
308.15	10000.00	0.8023	995.6
308.15	10000.00	0.8921	1022.7
308.15	10000.00	0.9478	1036.8
308.15	20000.00	0.0432	869.1
308.15	20000.00	0.1950	890.7
308.15	20000.00	0.3968	924.0
308.15	20000.00	0.4933	941.8
308.15	20000.00	0.5296	948.4
308.15	20000.00	0.5993	958.3
308.15	20000.00	0.7034	986.4
308.15	20000.00	0.8023	1004.4
308.15	20000.00	0.8921	1031.5
308.15	20000.00	0.9478	1045.7
308.15	30000.00	0.0432	875.7
308.15	30000.00	0.1950	897.5
308.15	30000.00	0.3968	931.2
308.15	30000.00	0.4933	949.4
308.15	30000.00	0.5296	956.0
308.15	30000.00	0.5993	970.9
308.15	30000.00	0.7034	994.2
308.15	30000.00	0.8023	1012.2
308.15	30000.00	0.8921	1039.7
308.15	30000.00	0.9478	1054.0
308.15	40000.00	0.0432	881.7
308.15	40000.00	0.1950	904.0
308.15	40000.00	0.3968	937.9
308.15	40000.00	0.4933	956.3
308.15	40000.00	0.5296	963.0
308.15	40000.00	0.5993	978.1
308.15	40000.00	0.7034	1001.5
308.15	40000.00	0.8023	1019.8
308.15	40000.00	0.8921	1047.4
308.15	40000.00	0.9478	1061.7

Mass density, kg/m3 [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	0.0432	871.8
288.15	100.00	0.1950	894.2
288.15	100.00	0.3968	924.2
288.15	100.00	0.4933	944.9
288.15	100.00	0.5296	953.3
288.15	100.00	0.5993	968.4
288.15	100.00	0.7034	992.3
288.15	100.00	0.8023	1010.6
288.15	100.00	0.8921	1038.1
288.15	100.00	0.9478	1052.9
288.15	5000.00	0.0432	875.5
288.15	5000.00	0.1950	897.8
288.15	5000.00	0.3968	931.9
288.15	5000.00	0.4933	950.4
288.15	5000.00	0.5296	957.3
288.15	5000.00	0.5993	972.4
288.15	5000.00	0.7034	996.2
288.15	5000.00	0.8023	1014.9
288.15	5000.00	0.8921	1042.5
288.15	5000.00	0.9478	1057.2
288.15	10000.00	0.0432	879.1
288.15	10000.00	0.1950	901.3
288.15	10000.00	0.3968	935.7
288.15	10000.00	0.4933	954.1
288.15	10000.00	0.5296	961.2
288.15	10000.00	0.5993	976.3
288.15	10000.00	0.7034	1000.3
288.15	10000.00	0.8023	1019.0
288.15	10000.00	0.8921	1046.6
288.15	10000.00	0.9478	1061.4
288.15	20000.00	0.0432	885.4
288.15	20000.00	0.1950	907.8
288.15	20000.00	0.3968	942.5
288.15	20000.00	0.4933	961.4
288.15	20000.00	0.5296	968.3
288.15	20000.00	0.5993	983.7
288.15	20000.00	0.7034	1007.8
288.15	20000.00	0.8023	1026.8
288.15	20000.00	0.8921	1054.5
288.15	20000.00	0.9478	1069.4
288.15	30000.00	0.0432	891.3
288.15	30000.00	0.1950	914.0
288.15	30000.00	0.3968	949.0
288.15	30000.00	0.4933	967.9
288.15	30000.00	0.5296	974.9
288.15	30000.00	0.5993	990.5
288.15	30000.00	0.7034	1014.7
288.15	30000.00	0.8023	1033.9
288.15	30000.00	0.8921	1061.5
288.15	30000.00	0.9478	1076.7
288.15	40000.00	0.0432	897.1
288.15	40000.00	0.1950	920.1
288.15	40000.00	0.3968	955.3
288.15	40000.00	0.4933	974.3
288.15	40000.00	0.5296	980.9
288.15	40000.00	0.5993	997.1
288.15	40000.00	0.7034	1021.4
288.15	40000.00	0.8023	1040.7
288.15	40000.00	0.8921	1068.7
288.15	40000.00	0.9478	1083.8
298.15	100.00	0.0432	863.0
298.15	100.00	0.1950	884.5
298.15	100.00	0.3968	917.8
298.15	100.00	0.4933	935.8
298.15	100.00	0.5296	942.5
298.15	100.00	0.5993	957.3
298.15	100.00	0.7034	980.5
298.15	100.00	0.8023	998.4
298.15	100.00	0.8921	1025.5
298.15	100.00	0.9478	1040.0
298.15	5000.00	0.0432	867.3
298.15	5000.00	0.1950	888.3
298.15	5000.00	0.3968	922.5
298.15	5000.00	0.4933	940.6
298.15	5000.00	0.5296	947.1
298.15	5000.00	0.5993	962.0
298.15	5000.00	0.7034	985.4
298.15	5000.00	0.8023	1003.4
298.15	5000.00	0.8921	1030.6
298.15	5000.00	0.9478	1044.9
298.15	10000.00	0.0432	870.4
298.15	10000.00	0.1950	892.1
298.15	10000.00	0.3968	925.8
298.15	10000.00	0.4933	944.0
298.15	10000.00	0.5296	950.7
298.15	10000.00	0.5993	965.7
298.15	10000.00	0.7034	989.1
298.15	10000.00	0.8023	1007.3
298.15	10000.00	0.8921	1034.7
298.15	10000.00	0.9478	1049.0
298.15	20000.00	0.0432	877.1
298.15	20000.00	0.1950	899.2
298.15	20000.00	0.3968	933.2
298.15	20000.00	0.4933	951.6
298.15	20000.00	0.5296	958.2
298.15	20000.00	0.5993	973.4
298.15	20000.00	0.7034	997.0
298.15	20000.00	0.8023	1015.5
298.15	20000.00	0.8921	1042.9
298.15	20000.00	0.9478	1057.5
298.15	30000.00	0.0432	883.4
298.15	30000.00	0.1950	905.5
298.15	30000.00	0.3968	939.9
298.15	30000.00	0.4933	958.7
298.15	30000.00	0.5296	965.4
298.15	30000.00	0.5993	980.5
298.15	30000.00	0.7034	1004.4
298.15	30000.00	0.8023	1022.7
298.15	30000.00	0.8921	1050.6
298.15	30000.00	0.9478	1065.0
298.15	40000.00	0.0432	889.1
298.15	40000.00	0.1950	911.7
298.15	40000.00	0.3968	946.5
298.15	40000.00	0.4933	965.1
298.15	40000.00	0.5296	972.0
298.15	40000.00	0.5993	987.3
298.15	40000.00	0.7034	1011.2
298.15	40000.00	0.8023	1030.1
298.15	40000.00	0.8921	1057.9
298.15	40000.00	0.9478	1072.7
308.15	100.00	0.0432	854.3
308.15	100.00	0.1950	875.2
308.15	100.00	0.3968	907.6
308.15	100.00	0.4933	925.2
308.15	100.00	0.5296	931.7
308.15	100.00	0.5993	946.3
308.15	100.00	0.7034	969.0
308.15	100.00	0.8023	986.4
308.15	100.00	0.8921	1013.1
308.15	100.00	0.9478	1027.2
308.15	5000.00	0.0432	858.1
308.15	5000.00	0.1950	879.3
308.15	5000.00	0.3968	912.1
308.15	5000.00	0.4933	929.7
308.15	5000.00	0.5296	936.2
308.15	5000.00	0.5993	950.8
308.15	5000.00	0.7034	973.7
308.15	5000.00	0.8023	991.0
308.15	5000.00	0.8921	1018.0
308.15	5000.00	0.9478	1032.1
308.15	10000.00	0.0432	862.0
308.15	10000.00	0.1950	883.3
308.15	10000.00	0.3968	916.2
308.15	10000.00	0.4933	934.1
308.15	10000.00	0.5296	940.4
308.15	10000.00	0.5993	955.2
308.15	10000.00	0.7034	978.2
308.15	10000.00	0.8023	995.6
308.15	10000.00	0.8921	1022.7
308.15	10000.00	0.9478	1036.8
308.15	20000.00	0.0432	869.1
308.15	20000.00	0.1950	890.7
308.15	20000.00	0.3968	924.0
308.15	20000.00	0.4933	941.8
308.15	20000.00	0.5296	948.4
308.15	20000.00	0.5993	958.3
308.15	20000.00	0.7034	986.4
308.15	20000.00	0.8023	1004.4
308.15	20000.00	0.8921	1031.5
308.15	20000.00	0.9478	1045.7
308.15	30000.00	0.0432	875.7
308.15	30000.00	0.1950	897.5
308.15	30000.00	0.3968	931.2
308.15	30000.00	0.4933	949.4
308.15	30000.00	0.5296	956.0
308.15	30000.00	0.5993	970.9
308.15	30000.00	0.7034	994.2
308.15	30000.00	0.8023	1012.2
308.15	30000.00	0.8921	1039.7
308.15	30000.00	0.9478	1054.0
308.15	40000.00	0.0432	881.7
308.15	40000.00	0.1950	904.0
308.15	40000.00	0.3968	937.9
308.15	40000.00	0.4933	956.3
308.15	40000.00	0.5296	963.0
308.15	40000.00	0.5993	978.1
308.15	40000.00	0.7034	1001.5
308.15	40000.00	0.8023	1019.8
308.15	40000.00	0.8921	1047.4
308.15	40000.00	0.9478	1061.7

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0503	0.0262
0.1937	0.0260
0.2988	0.0258
0.4013	0.0258
0.5016	0.0257
0.6032	0.0257
0.7029	0.0257
0.7964	0.0257
0.8945	0.0260
0.9442	0.0261

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0503	0.0262
0.1937	0.0260
0.2988	0.0258
0.4013	0.0258
0.5016	0.0257
0.6032	0.0257
0.7029	0.0257
0.7964	0.0257
0.8945	0.0260
0.9442	0.0261

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	363.35
0.8276	366.65
0.7037	370.05
0.6075	372.95
0.4878	377.25
0.4007	380.65
0.3192	384.45
0.2637	387.65
0.2102	391.05
0.1608	394.65
0.1197	398.25
0.0897	401.05
0.0675	403.25
0.0429	405.65
0.0240	407.95
0.0000	411.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of p-Xylene (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	360.73
0.0551	361.49
0.1334	362.26
0.2270	363.55
0.3045	364.62
0.3575	365.49
0.4678	367.65
0.5688	369.75
0.7372	376.35
0.8416	384.79
0.9369	396.71
0.9749	403.24
1.0000	408.37

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	363.35
0.8276	366.65
0.7037	370.05
0.6075	372.95
0.4878	377.25
0.4007	380.65
0.3192	384.45
0.2637	387.65
0.2102	391.05
0.1608	394.65
0.1197	398.25
0.0897	401.05
0.0675	403.25
0.0429	405.65
0.0240	407.95
0.0000	411.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 93.13 (Gas)

Mole fraction of p-Xylene (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	360.73
0.0551	361.49
0.1334	362.26
0.2270	363.55
0.3045	364.62
0.3575	365.49
0.4678	367.65
0.5688	369.75
0.7372	376.35
0.8416	384.79
0.9369	396.71
0.9749	403.24
1.0000	408.37

Sources

• Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
• Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
• Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
• 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
• Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K