Mixture of Methane, dibromo- + Heptane

Datasets

1. Azeotropic composition: mole fraction (4)
2. ρ_l - Mass density, kg/m3 (4)
3. c_sound,fluid - Speed of Sound, m/s (4)
4. Azeotropic pressure, kPa (4)

Azeotropic composition: mole fraction of Methane, dibromo- (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Methane, dibromo- (1) - Liquid
308.15	0.5567

Mole fraction of Methane, dibromo- (1) [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, dibromo- (1) - Liquid	Mole fraction of Methane, dibromo- (1) - Gas
0.1407	0.2854
0.2310	0.3807
0.3402	0.4616
0.4391	0.5131
0.5448	0.5555
0.5780	0.5663
0.5796	0.5676
0.6383	0.5887
0.6482	0.5900
0.6815	0.6069
0.7227	0.6175
0.7977	0.6442
0.8246	0.6712
0.8696	0.7005
0.9124	0.7433
0.9610	0.8274

Azeotropic composition: mole fraction of Methane, dibromo- (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Methane, dibromo- (1) - Liquid
308.15	0.5567

Mole fraction of Methane, dibromo- (1) [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, dibromo- (1) - Liquid	Mole fraction of Methane, dibromo- (1) - Gas
0.1407	0.2854
0.2310	0.3807
0.3402	0.4616
0.4391	0.5131
0.5448	0.5555
0.5780	0.5663
0.5796	0.5676
0.6383	0.5887
0.6482	0.5900
0.6815	0.6069
0.7227	0.6175
0.7977	0.6442
0.8246	0.6712
0.8696	0.7005
0.9124	0.7433
0.9610	0.8274

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Methane, dibromo- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	288.15	688.15
0.0000	293.15	683.94
0.0000	298.15	679.7
0.0000	303.15	675.44
0.0000	308.15	671.15
0.0000	313.15	666.83
0.0000	318.15	662.48
0.1019	288.15	779.65
0.1019	293.15	774.91
0.1019	298.15	770.15
0.1019	303.15	765.35
0.1019	308.15	760.52
0.1019	313.14	755.67
0.1019	318.15	750.77
0.1838	288.15	861.49
0.1838	293.15	856.29
0.1838	298.14	851.06
0.1838	303.15	845.79
0.1838	308.15	840.49
0.1838	313.15	835.16
0.1838	318.15	829.78
0.2536	288.15	937.65
0.2536	293.14	932.03
0.2536	298.14	926.36
0.2536	303.15	920.67
0.2536	308.15	914.94
0.2536	313.15	909.16
0.2536	318.15	903.35
0.3055	288.15	998.83
0.3055	293.15	992.87
0.3055	298.14	986.88
0.3055	303.15	980.85
0.3055	308.15	974.78
0.3055	313.15	968.68
0.3055	318.15	962.53
0.4064	288.15	1130.32
0.4064	293.14	1123.66
0.4064	298.15	1116.96
0.4064	303.15	1110.22
0.4064	308.15	1103.44
0.4064	313.15	1096.62
0.4064	318.15	1089.75
0.5029	288.15	1274.13
0.5029	293.15	1266.74
0.5029	298.15	1259.28
0.5029	303.15	1251.79
0.5029	308.15	1244.25
0.5029	313.14	1236.67
0.5029	318.15	1229.04
0.6023	288.15	1444.97
0.6023	293.14	1436.76
0.6023	298.14	1428.45
0.6023	303.14	1420.11
0.6023	308.15	1411.72
0.6023	313.15	1403.28
0.6023	318.15	1394.79
0.6525	288.15	1541.56
0.6525	293.15	1532.85
0.6525	298.15	1524.09
0.6525	303.15	1515.27
0.6525	308.15	1506.41
0.6525	313.14	1497.49
0.6525	318.15	1488.53
0.7016	288.15	1644.24
0.7016	293.14	1635.05
0.7016	298.14	1625.79
0.7016	303.15	1616.48
0.7016	308.15	1607.12
0.7016	313.15	1597.72
0.7016	318.15	1588.27
0.8003	288.15	1878.69
0.8003	293.15	1868.4
0.8003	298.15	1858.05
0.8003	303.15	1847.66
0.8003	308.15	1837.22
0.8003	313.15	1826.75
0.8003	318.15	1816.27
0.8961	288.15	2149.52
0.8961	293.15	2138.01
0.8961	298.14	2126.46
0.8961	303.15	2114.87
0.8961	308.15	2103.24
0.8961	313.15	2091.58
0.8961	318.15	2079.95
1.0000	288.15	2509.06
1.0000	293.15	2496.03
1.0000	298.15	2482.97
1.0000	303.15	2469.88
1.0000	308.15	2456.76
1.0000	313.15	2443.59
1.0000	318.15	2430.37

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	683.84
293.15	0.0504	727.59
293.15	0.1039	776.8
293.15	0.1552	826.84
293.15	0.2037	877.02
293.15	0.2532	931.38
293.15	0.3019	988.09
293.15	0.3540	1052.94
293.15	0.4022	1117.05
293.15	0.4552	1192.54
293.15	0.4962	1254.87
293.15	0.5532	1347.9
293.15	0.6119	1452.49
293.15	0.6543	1534.18
293.15	0.7032	1635.75
293.15	0.7514	1744.18
293.15	0.8024	1869.64
293.15	0.8518	2003.09
293.15	0.9004	2147.05
293.15	0.9502	2310.37
293.15	1.0000	2491.67
298.15	0.0000	679.6
298.15	0.0504	723.09
298.15	0.1039	772.01
298.15	0.1552	821.77
298.15	0.2037	871.66
298.15	0.2532	925.72
298.15	0.3019	982.12
298.15	0.3540	1046.61
298.15	0.4022	1110.37
298.15	0.4552	1185.46
298.15	0.4962	1247.47
298.15	0.5532	1339.98
298.15	0.6119	1444.09
298.15	0.6543	1525.37
298.15	0.7032	1626.46
298.15	0.7514	1734.39
298.15	0.8024	1859.25
298.15	0.8518	1992.14
298.15	0.9004	2135.43
298.15	0.9502	2298.08
298.15	1.0000	2478.61
303.15	0.0000	675.33
303.15	0.0504	718.56
303.15	0.1039	767.19
303.15	0.1552	816.67
303.15	0.2037	866.26
303.15	0.2532	920.03
303.15	0.3019	976.09
303.15	0.3540	1040.23
303.15	0.4022	1103.65
303.15	0.4552	1178.34
303.15	0.4962	1240.03
303.15	0.5532	1332.06
303.15	0.6119	1435.65
303.15	0.6543	1516.52
303.15	0.7032	1617.14
303.15	0.7514	1724.55
303.15	0.8024	1848.85
303.15	0.8518	1981.12
303.15	0.9004	2123.78
303.15	0.9502	2285.74
303.15	1.0000	2465.53
308.15	0.0000	671.04
308.15	0.0504	714.0
308.15	0.1039	762.36
308.15	0.1552	811.54
308.15	0.2037	860.84
308.15	0.2532	914.3
308.15	0.3019	970.04
308.15	0.3540	1033.82
308.15	0.4022	1096.88
308.15	0.4552	1171.15
308.15	0.4962	1232.54
308.15	0.5532	1324.08
308.15	0.6119	1427.16
308.15	0.6543	1507.63
308.15	0.7032	1607.76
308.15	0.7514	1714.66
308.15	0.8024	1838.4
308.15	0.8518	1970.07
308.15	0.9004	2112.21
308.15	0.9502	2273.36
308.15	1.0000	2452.42
313.15	0.0000	666.71
313.15	0.0504	709.41
313.15	0.1039	757.48
313.15	0.1552	806.36
313.15	0.2037	855.37
313.15	0.2532	908.53
313.15	0.3019	963.95
313.15	0.3540	1027.38
313.15	0.4022	1090.09
313.15	0.4552	1163.95
313.15	0.4962	1225.0
313.15	0.5532	1316.09
313.15	0.6119	1418.62
313.15	0.6543	1498.69
313.15	0.7032	1598.32
313.15	0.7514	1704.72
313.15	0.8024	1827.87
313.15	0.8518	1958.96
313.15	0.9004	2100.38
313.15	0.9502	2260.95
313.15	1.0000	2439.26

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Methane, dibromo- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	288.15	688.15
0.0000	293.15	683.94
0.0000	298.15	679.7
0.0000	303.15	675.44
0.0000	308.15	671.15
0.0000	313.15	666.83
0.0000	318.15	662.48
0.1019	288.15	779.65
0.1019	293.15	774.91
0.1019	298.15	770.15
0.1019	303.15	765.35
0.1019	308.15	760.52
0.1019	313.14	755.67
0.1019	318.15	750.77
0.1838	288.15	861.49
0.1838	293.15	856.29
0.1838	298.14	851.06
0.1838	303.15	845.79
0.1838	308.15	840.49
0.1838	313.15	835.16
0.1838	318.15	829.78
0.2536	288.15	937.65
0.2536	293.14	932.03
0.2536	298.14	926.36
0.2536	303.15	920.67
0.2536	308.15	914.94
0.2536	313.15	909.16
0.2536	318.15	903.35
0.3055	288.15	998.83
0.3055	293.15	992.87
0.3055	298.14	986.88
0.3055	303.15	980.85
0.3055	308.15	974.78
0.3055	313.15	968.68
0.3055	318.15	962.53
0.4064	288.15	1130.32
0.4064	293.14	1123.66
0.4064	298.15	1116.96
0.4064	303.15	1110.22
0.4064	308.15	1103.44
0.4064	313.15	1096.62
0.4064	318.15	1089.75
0.5029	288.15	1274.13
0.5029	293.15	1266.74
0.5029	298.15	1259.28
0.5029	303.15	1251.79
0.5029	308.15	1244.25
0.5029	313.14	1236.67
0.5029	318.15	1229.04
0.6023	288.15	1444.97
0.6023	293.14	1436.76
0.6023	298.14	1428.45
0.6023	303.14	1420.11
0.6023	308.15	1411.72
0.6023	313.15	1403.28
0.6023	318.15	1394.79
0.6525	288.15	1541.56
0.6525	293.15	1532.85
0.6525	298.15	1524.09
0.6525	303.15	1515.27
0.6525	308.15	1506.41
0.6525	313.14	1497.49
0.6525	318.15	1488.53
0.7016	288.15	1644.24
0.7016	293.14	1635.05
0.7016	298.14	1625.79
0.7016	303.15	1616.48
0.7016	308.15	1607.12
0.7016	313.15	1597.72
0.7016	318.15	1588.27
0.8003	288.15	1878.69
0.8003	293.15	1868.4
0.8003	298.15	1858.05
0.8003	303.15	1847.66
0.8003	308.15	1837.22
0.8003	313.15	1826.75
0.8003	318.15	1816.27
0.8961	288.15	2149.52
0.8961	293.15	2138.01
0.8961	298.14	2126.46
0.8961	303.15	2114.87
0.8961	308.15	2103.24
0.8961	313.15	2091.58
0.8961	318.15	2079.95
1.0000	288.15	2509.06
1.0000	293.15	2496.03
1.0000	298.15	2482.97
1.0000	303.15	2469.88
1.0000	308.15	2456.76
1.0000	313.15	2443.59
1.0000	318.15	2430.37

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	683.84
293.15	0.0504	727.59
293.15	0.1039	776.8
293.15	0.1552	826.84
293.15	0.2037	877.02
293.15	0.2532	931.38
293.15	0.3019	988.09
293.15	0.3540	1052.94
293.15	0.4022	1117.05
293.15	0.4552	1192.54
293.15	0.4962	1254.87
293.15	0.5532	1347.9
293.15	0.6119	1452.49
293.15	0.6543	1534.18
293.15	0.7032	1635.75
293.15	0.7514	1744.18
293.15	0.8024	1869.64
293.15	0.8518	2003.09
293.15	0.9004	2147.05
293.15	0.9502	2310.37
293.15	1.0000	2491.67
298.15	0.0000	679.6
298.15	0.0504	723.09
298.15	0.1039	772.01
298.15	0.1552	821.77
298.15	0.2037	871.66
298.15	0.2532	925.72
298.15	0.3019	982.12
298.15	0.3540	1046.61
298.15	0.4022	1110.37
298.15	0.4552	1185.46
298.15	0.4962	1247.47
298.15	0.5532	1339.98
298.15	0.6119	1444.09
298.15	0.6543	1525.37
298.15	0.7032	1626.46
298.15	0.7514	1734.39
298.15	0.8024	1859.25
298.15	0.8518	1992.14
298.15	0.9004	2135.43
298.15	0.9502	2298.08
298.15	1.0000	2478.61
303.15	0.0000	675.33
303.15	0.0504	718.56
303.15	0.1039	767.19
303.15	0.1552	816.67
303.15	0.2037	866.26
303.15	0.2532	920.03
303.15	0.3019	976.09
303.15	0.3540	1040.23
303.15	0.4022	1103.65
303.15	0.4552	1178.34
303.15	0.4962	1240.03
303.15	0.5532	1332.06
303.15	0.6119	1435.65
303.15	0.6543	1516.52
303.15	0.7032	1617.14
303.15	0.7514	1724.55
303.15	0.8024	1848.85
303.15	0.8518	1981.12
303.15	0.9004	2123.78
303.15	0.9502	2285.74
303.15	1.0000	2465.53
308.15	0.0000	671.04
308.15	0.0504	714.0
308.15	0.1039	762.36
308.15	0.1552	811.54
308.15	0.2037	860.84
308.15	0.2532	914.3
308.15	0.3019	970.04
308.15	0.3540	1033.82
308.15	0.4022	1096.88
308.15	0.4552	1171.15
308.15	0.4962	1232.54
308.15	0.5532	1324.08
308.15	0.6119	1427.16
308.15	0.6543	1507.63
308.15	0.7032	1607.76
308.15	0.7514	1714.66
308.15	0.8024	1838.4
308.15	0.8518	1970.07
308.15	0.9004	2112.21
308.15	0.9502	2273.36
308.15	1.0000	2452.42
313.15	0.0000	666.71
313.15	0.0504	709.41
313.15	0.1039	757.48
313.15	0.1552	806.36
313.15	0.2037	855.37
313.15	0.2532	908.53
313.15	0.3019	963.95
313.15	0.3540	1027.38
313.15	0.4022	1090.09
313.15	0.4552	1163.95
313.15	0.4962	1225.0
313.15	0.5532	1316.09
313.15	0.6119	1418.62
313.15	0.6543	1498.69
313.15	0.7032	1598.32
313.15	0.7514	1704.72
313.15	0.8024	1827.87
313.15	0.8518	1958.96
313.15	0.9004	2100.38
313.15	0.9502	2260.95
313.15	1.0000	2439.26

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Methane, dibromo- (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0000	292.87	1152.55
0.0000	298.14	1129.65
0.0000	303.12	1108.21
0.0000	308.10	1086.83
0.0000	313.27	1064.73
0.1062	292.89	1103.98
0.1062	298.16	1082.36
0.1062	303.13	1062.09
0.1062	308.12	1041.86
0.1062	313.29	1021.0
0.2032	292.89	1066.26
0.2032	298.15	1045.83
0.2032	303.13	1026.62
0.2032	308.10	1007.5
0.2032	313.28	987.55
0.3040	292.89	1032.13
0.3040	298.16	1012.68
0.3040	303.13	994.46
0.3040	308.12	976.3
0.3040	313.30	957.58
0.4050	292.90	1002.43
0.4050	298.18	984.03
0.4050	303.15	966.75
0.4050	308.13	949.39
0.4050	313.31	931.52
0.4998	292.90	979.49
0.4998	298.17	962.0
0.4998	303.15	945.56
0.4998	308.12	929.18
0.4998	313.31	912.23
0.6048	292.92	959.47
0.6048	298.19	942.98
0.6048	303.17	927.45
0.6048	308.14	911.94
0.6048	313.32	895.85
0.7043	292.91	946.92
0.7043	298.18	931.29
0.7043	303.15	916.56
0.7043	308.14	901.84
0.7043	313.31	886.55
0.8031	292.91	941.84
0.8031	298.17	926.99
0.8031	303.14	913.0
0.8031	308.13	899.01
0.8031	313.31	884.49
0.9019	292.88	946.13
0.9019	298.15	931.96
0.9019	303.13	918.63
0.9019	308.11	905.33
0.9019	313.28	891.54
1.0000	292.87	960.63
1.0000	298.15	947.15
1.0000	303.11	934.52
1.0000	308.10	921.89
1.0000	313.27	908.83

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, dibromo- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1152.2
293.15	0.0504	1128.1
293.15	0.1039	1104.9
293.15	0.1552	1084.0
293.15	0.2037	1065.7
293.15	0.2532	1048.3
293.15	0.3019	1032.4
293.15	0.3540	1016.7
293.15	0.4022	1003.5
293.15	0.4552	990.1
293.15	0.4962	980.6
293.15	0.5532	969.3
293.15	0.6119	959.2
293.15	0.6543	953.4
293.15	0.7032	948.0
293.15	0.7514	944.6
293.15	0.8024	942.9
293.15	0.8518	943.8
293.15	0.9004	947.2
293.15	0.9502	953.1
293.15	1.0000	961.8
298.15	0.0000	1130.9
298.15	0.0504	1107.3
298.15	0.1039	1084.7
298.15	0.1552	1064.4
298.15	0.2037	1046.5
298.15	0.2532	1029.7
298.15	0.3019	1014.2
298.15	0.3540	999.1
298.15	0.4022	986.1
298.15	0.4552	973.2
298.15	0.4962	964.2
298.15	0.5532	953.3
298.15	0.6119	943.8
298.15	0.6543	938.2
298.15	0.7032	933.3
298.15	0.7514	930.2
298.15	0.8024	928.9
298.15	0.8518	930.2
298.15	0.9004	933.8
298.15	0.9502	940.1
298.15	1.0000	949.2
303.15	0.0000	1109.1
303.15	0.0504	1086.4
303.15	0.1039	1064.4
303.15	0.1552	1044.8
303.15	0.2037	1027.3
303.15	0.2532	1010.9
303.15	0.3019	995.8
303.15	0.3540	981.2
303.15	0.4022	968.8
303.15	0.4552	956.4
303.15	0.4962	947.8
303.15	0.5532	937.4
303.15	0.6119	928.3
303.15	0.6543	923.1
303.15	0.7032	918.6
303.15	0.7514	915.8
303.15	0.8024	915.0
303.15	0.8518	916.5
303.15	0.9004	920.3
303.15	0.9502	927.1
303.15	1.0000	936.6
308.15	0.0000	1088.1
308.15	0.0504	1065.7
308.15	0.1039	1044.3
308.15	0.1552	1025.2
308.15	0.2037	1008.2
308.15	0.2532	992.3
308.15	0.3019	977.6
308.15	0.3540	963.5
308.15	0.4022	951.5
308.15	0.4552	939.6
308.15	0.4962	931.2
308.15	0.5532	921.4
308.15	0.6119	912.9
308.15	0.6543	908.0
308.15	0.7032	903.9
308.15	0.7514	901.5
308.15	0.8024	901.1
308.15	0.8518	902.9
308.15	0.9004	907.1
308.15	0.9502	914.1
308.15	1.0000	924.0
313.15	0.0000	1066.9
313.15	0.0504	1045.1
313.15	0.1039	1024.3
313.15	0.1552	1005.6
313.15	0.2037	989.0
313.15	0.2532	973.7
313.15	0.3019	959.6
313.15	0.3540	946.0
313.15	0.4022	934.5
313.15	0.4552	923.0
313.15	0.4962	914.8
313.15	0.5532	905.5
313.15	0.6119	897.5
313.15	0.6543	893.0
313.15	0.7032	889.2
313.15	0.7514	887.2
313.15	0.8024	887.0
313.15	0.8518	889.3
313.15	0.9004	893.8
313.15	0.9502	901.1
313.15	1.0000	911.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Methane, dibromo- (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0000	292.87	1152.55
0.0000	298.14	1129.65
0.0000	303.12	1108.21
0.0000	308.10	1086.83
0.0000	313.27	1064.73
0.1062	292.89	1103.98
0.1062	298.16	1082.36
0.1062	303.13	1062.09
0.1062	308.12	1041.86
0.1062	313.29	1021.0
0.2032	292.89	1066.26
0.2032	298.15	1045.83
0.2032	303.13	1026.62
0.2032	308.10	1007.5
0.2032	313.28	987.55
0.3040	292.89	1032.13
0.3040	298.16	1012.68
0.3040	303.13	994.46
0.3040	308.12	976.3
0.3040	313.30	957.58
0.4050	292.90	1002.43
0.4050	298.18	984.03
0.4050	303.15	966.75
0.4050	308.13	949.39
0.4050	313.31	931.52
0.4998	292.90	979.49
0.4998	298.17	962.0
0.4998	303.15	945.56
0.4998	308.12	929.18
0.4998	313.31	912.23
0.6048	292.92	959.47
0.6048	298.19	942.98
0.6048	303.17	927.45
0.6048	308.14	911.94
0.6048	313.32	895.85
0.7043	292.91	946.92
0.7043	298.18	931.29
0.7043	303.15	916.56
0.7043	308.14	901.84
0.7043	313.31	886.55
0.8031	292.91	941.84
0.8031	298.17	926.99
0.8031	303.14	913.0
0.8031	308.13	899.01
0.8031	313.31	884.49
0.9019	292.88	946.13
0.9019	298.15	931.96
0.9019	303.13	918.63
0.9019	308.11	905.33
0.9019	313.28	891.54
1.0000	292.87	960.63
1.0000	298.15	947.15
1.0000	303.11	934.52
1.0000	308.10	921.89
1.0000	313.27	908.83

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methane, dibromo- (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1152.2
293.15	0.0504	1128.1
293.15	0.1039	1104.9
293.15	0.1552	1084.0
293.15	0.2037	1065.7
293.15	0.2532	1048.3
293.15	0.3019	1032.4
293.15	0.3540	1016.7
293.15	0.4022	1003.5
293.15	0.4552	990.1
293.15	0.4962	980.6
293.15	0.5532	969.3
293.15	0.6119	959.2
293.15	0.6543	953.4
293.15	0.7032	948.0
293.15	0.7514	944.6
293.15	0.8024	942.9
293.15	0.8518	943.8
293.15	0.9004	947.2
293.15	0.9502	953.1
293.15	1.0000	961.8
298.15	0.0000	1130.9
298.15	0.0504	1107.3
298.15	0.1039	1084.7
298.15	0.1552	1064.4
298.15	0.2037	1046.5
298.15	0.2532	1029.7
298.15	0.3019	1014.2
298.15	0.3540	999.1
298.15	0.4022	986.1
298.15	0.4552	973.2
298.15	0.4962	964.2
298.15	0.5532	953.3
298.15	0.6119	943.8
298.15	0.6543	938.2
298.15	0.7032	933.3
298.15	0.7514	930.2
298.15	0.8024	928.9
298.15	0.8518	930.2
298.15	0.9004	933.8
298.15	0.9502	940.1
298.15	1.0000	949.2
303.15	0.0000	1109.1
303.15	0.0504	1086.4
303.15	0.1039	1064.4
303.15	0.1552	1044.8
303.15	0.2037	1027.3
303.15	0.2532	1010.9
303.15	0.3019	995.8
303.15	0.3540	981.2
303.15	0.4022	968.8
303.15	0.4552	956.4
303.15	0.4962	947.8
303.15	0.5532	937.4
303.15	0.6119	928.3
303.15	0.6543	923.1
303.15	0.7032	918.6
303.15	0.7514	915.8
303.15	0.8024	915.0
303.15	0.8518	916.5
303.15	0.9004	920.3
303.15	0.9502	927.1
303.15	1.0000	936.6
308.15	0.0000	1088.1
308.15	0.0504	1065.7
308.15	0.1039	1044.3
308.15	0.1552	1025.2
308.15	0.2037	1008.2
308.15	0.2532	992.3
308.15	0.3019	977.6
308.15	0.3540	963.5
308.15	0.4022	951.5
308.15	0.4552	939.6
308.15	0.4962	931.2
308.15	0.5532	921.4
308.15	0.6119	912.9
308.15	0.6543	908.0
308.15	0.7032	903.9
308.15	0.7514	901.5
308.15	0.8024	901.1
308.15	0.8518	902.9
308.15	0.9004	907.1
308.15	0.9502	914.1
308.15	1.0000	924.0
313.15	0.0000	1066.9
313.15	0.0504	1045.1
313.15	0.1039	1024.3
313.15	0.1552	1005.6
313.15	0.2037	989.0
313.15	0.2532	973.7
313.15	0.3019	959.6
313.15	0.3540	946.0
313.15	0.4022	934.5
313.15	0.4552	923.0
313.15	0.4962	914.8
313.15	0.5532	905.5
313.15	0.6119	897.5
313.15	0.6543	893.0
313.15	0.7032	889.2
313.15	0.7514	887.2
313.15	0.8024	887.0
313.15	0.8518	889.3
313.15	0.9004	893.8
313.15	0.9502	901.1
313.15	1.0000	911.4

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
308.15	14.08

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, dibromo- (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.1407	12.20
0.2310	13.03
0.3402	13.68
0.4391	14.00
0.5448	14.08
0.5780	14.07
0.5796	14.09
0.6383	14.05
0.6482	14.03
0.6815	13.97
0.7227	13.87
0.7977	13.61
0.8246	13.47
0.8696	13.17
0.9124	12.74
0.9610	11.76

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
308.15	14.08

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 308.15 (Liquid)

Mole fraction of Methane, dibromo- (1) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.1407	12.20
0.2310	13.03
0.3402	13.68
0.4391	14.00
0.5448	14.08
0.5780	14.07
0.5796	14.09
0.6383	14.05
0.6482	14.03
0.6815	13.97
0.7227	13.87
0.7977	13.61
0.8246	13.47
0.8696	13.17
0.9124	12.74
0.9610	11.76

Sources

• Thermodynamic and Acoustic Properties of Mixtures of Dibromomethane + Heptane
• Vapour liquid equilibrium at T = 308.15 K for binary systems: Dibromomethane + n-heptane, bromotrichloromethane + n-heptane, bromotrichloromethane + dibromomethane, bromotrichloromethane + bromochloromethane and dibromomethane + bromochloromethane. Experimental data and modelling
• Excess Molar Volumes and Speed of Sound in Bromotrichloromethane + n-Heptane, Dibromomethane + n-Heptane, Bromotrichloromethane + Dibromomethane, and Bromotrichloromethane + Bromochloromethane at Temperatures from (293.15 to 313.15) K