Mixture of Propylene Carbonate + Benzene, 1,3-dimethyl-

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 Benzene, 1,3-dimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1200.25
293.15	0.0576	1173.76
293.15	0.1263	1143.64
293.15	0.1735	1123.83
293.15	0.2267	1102.36
293.15	0.2867	1079.14
293.15	0.3548	1054.0
293.15	0.4243	1029.6
293.15	0.4671	1015.15
293.15	0.5341	993.4
293.15	0.5811	978.7
293.15	0.6532	957.01
293.15	0.7213	937.38
293.15	0.7831	920.23
293.15	0.8421	904.39
293.15	0.9212	883.89
293.15	1.0000	864.2
303.15	0.0000	1180.56
303.15	0.0476	1159.4
303.15	0.1178	1129.53
303.15	0.1822	1103.48
303.15	0.2248	1086.93
303.15	0.2978	1059.75
303.15	0.3681	1034.91
303.15	0.4348	1012.48
303.15	0.5038	990.33
303.15	0.5598	973.11
303.15	0.6139	957.05
303.15	0.6738	939.89
303.15	0.7355	922.85
303.15	0.8021	905.11
303.15	0.8837	884.19
303.15	0.9475	868.42
303.15	1.0000	855.76
313.15	0.0000	1161.28
313.15	0.0564	1137.19
313.15	0.1291	1107.58
313.15	0.1781	1088.5
313.15	0.2378	1066.16
313.15	0.3021	1043.18
313.15	0.3614	1022.91
313.15	0.4243	1002.32
313.15	0.4861	982.96
313.15	0.5349	968.22
313.15	0.5924	951.44
313.15	0.6521	934.66
313.15	0.7134	918.04
313.15	0.7634	904.91
313.15	0.8325	887.34
313.15	0.9334	862.75
313.15	1.0000	847.11
323.15	0.0000	1142.43
323.15	0.0525	1120.74
323.15	0.1203	1093.93
323.15	0.1832	1070.24
323.15	0.2498	1046.31
323.15	0.3103	1025.54
323.15	0.3667	1006.98
323.15	0.4327	986.16
323.15	0.4962	967.01
323.15	0.5587	948.93
323.15	0.6148	933.3
323.15	0.6813	915.46
323.15	0.7539	896.75
323.15	0.8013	884.94
323.15	0.8625	870.1
323.15	0.9346	853.17
323.15	1.0000	838.27
333.15	0.0000	1123.99
333.15	0.0478	1104.87
333.15	0.1249	1075.39
333.15	0.1942	1050.25
333.15	0.2571	1028.52
333.15	0.3245	1006.29
333.15	0.3878	986.36
333.15	0.4313	973.16
333.15	0.5138	949.16
333.15	0.5820	930.28
333.15	0.6842	903.43
333.15	0.7323	891.34
333.15	0.7723	881.53
333.15	0.8248	868.96
333.15	0.8833	855.34
333.15	0.9429	841.84
333.15	1.0000	829.22
343.15	0.0000	1105.98
343.15	0.0634	1081.55
343.15	0.1278	1057.84
343.15	0.1798	1039.5
343.15	0.2348	1020.82
343.15	0.3013	999.21
343.15	0.3703	977.83
343.15	0.4259	961.33
343.15	0.4829	945.05
343.15	0.5329	931.26
343.15	0.5928	915.31
343.15	0.6528	899.92
343.15	0.7132	884.96
343.15	0.7829	868.32
343.15	0.8532	852.13
343.15	0.9253	836.07
343.15	1.0000	819.97
353.15	0.0000	1088.38
353.15	0.0622	1065.11
353.15	0.1199	1044.44
353.15	0.1874	1021.32
353.15	0.2401	1004.03
353.15	0.3149	980.58
353.15	0.3871	959.07
353.15	0.4510	940.91
353.15	0.5249	920.84
353.15	0.5832	905.67
353.15	0.6591	886.72
353.15	0.7249	870.97
353.15	0.7719	860.05
353.15	0.8529	841.86
353.15	0.8941	832.88
353.15	0.9483	821.31
353.15	1.0000	810.51

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Benzene, 1,3-dimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	1200.25
293.15	0.0576	1173.76
293.15	0.1263	1143.64
293.15	0.1735	1123.83
293.15	0.2267	1102.36
293.15	0.2867	1079.14
293.15	0.3548	1054.0
293.15	0.4243	1029.6
293.15	0.4671	1015.15
293.15	0.5341	993.4
293.15	0.5811	978.7
293.15	0.6532	957.01
293.15	0.7213	937.38
293.15	0.7831	920.23
293.15	0.8421	904.39
293.15	0.9212	883.89
293.15	1.0000	864.2
303.15	0.0000	1180.56
303.15	0.0476	1159.4
303.15	0.1178	1129.53
303.15	0.1822	1103.48
303.15	0.2248	1086.93
303.15	0.2978	1059.75
303.15	0.3681	1034.91
303.15	0.4348	1012.48
303.15	0.5038	990.33
303.15	0.5598	973.11
303.15	0.6139	957.05
303.15	0.6738	939.89
303.15	0.7355	922.85
303.15	0.8021	905.11
303.15	0.8837	884.19
303.15	0.9475	868.42
303.15	1.0000	855.76
313.15	0.0000	1161.28
313.15	0.0564	1137.19
313.15	0.1291	1107.58
313.15	0.1781	1088.5
313.15	0.2378	1066.16
313.15	0.3021	1043.18
313.15	0.3614	1022.91
313.15	0.4243	1002.32
313.15	0.4861	982.96
313.15	0.5349	968.22
313.15	0.5924	951.44
313.15	0.6521	934.66
313.15	0.7134	918.04
313.15	0.7634	904.91
313.15	0.8325	887.34
313.15	0.9334	862.75
313.15	1.0000	847.11
323.15	0.0000	1142.43
323.15	0.0525	1120.74
323.15	0.1203	1093.93
323.15	0.1832	1070.24
323.15	0.2498	1046.31
323.15	0.3103	1025.54
323.15	0.3667	1006.98
323.15	0.4327	986.16
323.15	0.4962	967.01
323.15	0.5587	948.93
323.15	0.6148	933.3
323.15	0.6813	915.46
323.15	0.7539	896.75
323.15	0.8013	884.94
323.15	0.8625	870.1
323.15	0.9346	853.17
323.15	1.0000	838.27
333.15	0.0000	1123.99
333.15	0.0478	1104.87
333.15	0.1249	1075.39
333.15	0.1942	1050.25
333.15	0.2571	1028.52
333.15	0.3245	1006.29
333.15	0.3878	986.36
333.15	0.4313	973.16
333.15	0.5138	949.16
333.15	0.5820	930.28
333.15	0.6842	903.43
333.15	0.7323	891.34
333.15	0.7723	881.53
333.15	0.8248	868.96
333.15	0.8833	855.34
333.15	0.9429	841.84
333.15	1.0000	829.22
343.15	0.0000	1105.98
343.15	0.0634	1081.55
343.15	0.1278	1057.84
343.15	0.1798	1039.5
343.15	0.2348	1020.82
343.15	0.3013	999.21
343.15	0.3703	977.83
343.15	0.4259	961.33
343.15	0.4829	945.05
343.15	0.5329	931.26
343.15	0.5928	915.31
343.15	0.6528	899.92
343.15	0.7132	884.96
343.15	0.7829	868.32
343.15	0.8532	852.13
343.15	0.9253	836.07
343.15	1.0000	819.97
353.15	0.0000	1088.38
353.15	0.0622	1065.11
353.15	0.1199	1044.44
353.15	0.1874	1021.32
353.15	0.2401	1004.03
353.15	0.3149	980.58
353.15	0.3871	959.07
353.15	0.4510	940.91
353.15	0.5249	920.84
353.15	0.5832	905.67
353.15	0.6591	886.72
353.15	0.7249	870.97
353.15	0.7719	860.05
353.15	0.8529	841.86
353.15	0.8941	832.88
353.15	0.9483	821.31
353.15	1.0000	810.51

Sources

• Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K