Mixture of Propylene Carbonate + Ethylbenzene

Datasets

1. ρ_l - Mass density, kg/m3 (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1200.3
303.15	0.0000	1180.6
313.15	0.0000	1161.3
323.15	0.0000	1142.4
333.15	0.0000	1124.0
343.15	0.0000	1106.0
353.15	0.0000	1088.4
303.15	0.0489	1159.1
343.15	0.0524	1088.2
333.15	0.0587	1102.4
293.15	0.0592	1173.5
353.15	0.0629	1069.2
323.15	0.0635	1117.4
313.15	0.0662	1133.7
343.15	0.1125	1068.5
293.15	0.1139	1149.9
323.15	0.1139	1098.3
313.15	0.1258	1110.0
353.15	0.1272	1050.2
303.15	0.1278	1126.2
333.15	0.1328	1076.2
323.15	0.1729	1076.8
293.15	0.1749	1124.6
343.15	0.1828	1046.3
313.15	0.1835	1088.0
333.15	0.1849	1058.6
353.15	0.1947	1031.0
303.15	0.1974	1098.6
323.15	0.2384	1054.0
343.15	0.2398	1029.1
313.15	0.2458	1065.3
293.15	0.2471	1096.1
303.15	0.2484	1079.4
333.15	0.2489	1037.9
353.15	0.2598	1013.3
343.15	0.3049	1010.2
353.15	0.3138	999.0
303.15	0.3149	1055.2
333.15	0.3186	1016.2
323.15	0.3248	1025.4
293.15	0.3274	1066.1
313.15	0.3342	1034.7
343.15	0.3673	992.8
303.15	0.3759	1034.1
333.15	0.3767	998.9
293.15	0.3856	1045.5
323.15	0.3859	1006.2
353.15	0.3945	978.6
313.15	0.3958	1014.5
343.15	0.4348	974.7
303.15	0.4349	1014.5
333.15	0.4350	982.2
323.15	0.4523	986.2
293.15	0.4527	1022.7
313.15	0.4592	994.6
353.15	0.4629	962.0
343.15	0.4817	962.6
303.15	0.4876	997.7
333.15	0.4957	965.5
323.15	0.5048	971.0
293.15	0.5049	1005.6
313.15	0.5135	978.2
353.15	0.5148	949.8
343.15	0.5428	947.3
303.15	0.5498	978.5
333.15	0.5549	949.7
313.15	0.5629	963.7
293.15	0.5672	986.1
323.15	0.5733	951.9
353.15	0.5749	936.1
303.15	0.5922	965.9
343.15	0.6048	932.3
333.15	0.6247	931.8
313.15	0.6248	946.2
353.15	0.6345	923.0
293.15	0.6368	965.1
323.15	0.6387	934.4
303.15	0.6590	946.7
343.15	0.6721	916.5
313.15	0.6724	933.2
333.15	0.6978	913.8
293.15	0.6978	947.4
323.15	0.7038	917.6
353.15	0.7039	908.2
303.15	0.7249	928.4
313.15	0.7383	915.7
343.15	0.7498	899.0
293.15	0.7529	932.0
323.15	0.7587	903.8
333.15	0.7629	898.4
353.15	0.7635	895.8
313.15	0.7873	903.2
303.15	0.7941	910.0
323.15	0.8137	890.5
353.15	0.8137	885.7
293.15	0.8149	915.2
343.15	0.8247	882.7
333.15	0.8247	884.2
313.15	0.8534	886.7
303.15	0.8578	893.5
333.15	0.8624	875.7
353.15	0.8642	875.7
323.15	0.8698	877.2
293.15	0.8742	899.6
343.15	0.8827	870.5
303.15	0.9247	876.8
323.15	0.9247	864.5
353.15	0.9248	863.9
333.15	0.9358	859.5
293.15	0.9368	883.5
313.15	0.9378	866.4
343.15	0.9478	857.0
323.15	1.0000	847.6
293.15	1.0000	867.8
303.15	1.0000	858.6
333.15	1.0000	845.8
343.15	1.0000	846.5
313.15	1.0000	851.8
353.15	1.0000	849.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylbenzene (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1200.3
303.15	0.0000	1180.6
313.15	0.0000	1161.3
323.15	0.0000	1142.4
333.15	0.0000	1124.0
343.15	0.0000	1106.0
353.15	0.0000	1088.4
303.15	0.0489	1159.1
343.15	0.0524	1088.2
333.15	0.0587	1102.4
293.15	0.0592	1173.5
353.15	0.0629	1069.2
323.15	0.0635	1117.4
313.15	0.0662	1133.7
343.15	0.1125	1068.5
293.15	0.1139	1149.9
323.15	0.1139	1098.3
313.15	0.1258	1110.0
353.15	0.1272	1050.2
303.15	0.1278	1126.2
333.15	0.1328	1076.2
323.15	0.1729	1076.8
293.15	0.1749	1124.6
343.15	0.1828	1046.3
313.15	0.1835	1088.0
333.15	0.1849	1058.6
353.15	0.1947	1031.0
303.15	0.1974	1098.6
323.15	0.2384	1054.0
343.15	0.2398	1029.1
313.15	0.2458	1065.3
293.15	0.2471	1096.1
303.15	0.2484	1079.4
333.15	0.2489	1037.9
353.15	0.2598	1013.3
343.15	0.3049	1010.2
353.15	0.3138	999.0
303.15	0.3149	1055.2
333.15	0.3186	1016.2
323.15	0.3248	1025.4
293.15	0.3274	1066.1
313.15	0.3342	1034.7
343.15	0.3673	992.8
303.15	0.3759	1034.1
333.15	0.3767	998.9
293.15	0.3856	1045.5
323.15	0.3859	1006.2
353.15	0.3945	978.6
313.15	0.3958	1014.5
343.15	0.4348	974.7
303.15	0.4349	1014.5
333.15	0.4350	982.2
323.15	0.4523	986.2
293.15	0.4527	1022.7
313.15	0.4592	994.6
353.15	0.4629	962.0
343.15	0.4817	962.6
303.15	0.4876	997.7
333.15	0.4957	965.5
323.15	0.5048	971.0
293.15	0.5049	1005.6
313.15	0.5135	978.2
353.15	0.5148	949.8
343.15	0.5428	947.3
303.15	0.5498	978.5
333.15	0.5549	949.7
313.15	0.5629	963.7
293.15	0.5672	986.1
323.15	0.5733	951.9
353.15	0.5749	936.1
303.15	0.5922	965.9
343.15	0.6048	932.3
333.15	0.6247	931.8
313.15	0.6248	946.2
353.15	0.6345	923.0
293.15	0.6368	965.1
323.15	0.6387	934.4
303.15	0.6590	946.7
343.15	0.6721	916.5
313.15	0.6724	933.2
333.15	0.6978	913.8
293.15	0.6978	947.4
323.15	0.7038	917.6
353.15	0.7039	908.2
303.15	0.7249	928.4
313.15	0.7383	915.7
343.15	0.7498	899.0
293.15	0.7529	932.0
323.15	0.7587	903.8
333.15	0.7629	898.4
353.15	0.7635	895.8
313.15	0.7873	903.2
303.15	0.7941	910.0
323.15	0.8137	890.5
353.15	0.8137	885.7
293.15	0.8149	915.2
343.15	0.8247	882.7
333.15	0.8247	884.2
313.15	0.8534	886.7
303.15	0.8578	893.5
333.15	0.8624	875.7
353.15	0.8642	875.7
323.15	0.8698	877.2
293.15	0.8742	899.6
343.15	0.8827	870.5
303.15	0.9247	876.8
323.15	0.9247	864.5
353.15	0.9248	863.9
333.15	0.9358	859.5
293.15	0.9368	883.5
313.15	0.9378	866.4
343.15	0.9478	857.0
323.15	1.0000	847.6
293.15	1.0000	867.8
303.15	1.0000	858.6
333.15	1.0000	845.8
343.15	1.0000	846.5
313.15	1.0000	851.8
353.15	1.0000	849.6

Sources

• The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K