Mixture of Methane, bromochloro- + Ethyl Acetate

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. ρ_l - Mass density, kg/m3 (2)

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

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methane, bromochloro- (1) - Liquid	Mole fraction of Methane, bromochloro- (1) - Gas
0.0887	0.0898
0.1583	0.1661
0.2451	0.2686
0.3372	0.3789
0.4046	0.4535
0.4370	0.4973
0.4901	0.5788
0.5083	0.6072
0.5445	0.6460
0.7428	0.8413
0.7916	0.8801
0.8362	0.9116
0.9274	0.9644

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

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methane, bromochloro- (1) - Liquid	Mole fraction of Methane, bromochloro- (1) - Gas
0.0887	0.0898
0.1583	0.1661
0.2451	0.2686
0.3372	0.3789
0.4046	0.4535
0.4370	0.4973
0.4901	0.5788
0.5083	0.6072
0.5445	0.6460
0.7428	0.8413
0.7916	0.8801
0.8362	0.9116
0.9274	0.9644

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methane, bromochloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0887	25.40
0.1583	25.52
0.2451	25.85
0.3372	26.35
0.4046	26.93
0.4370	27.22
0.4901	27.85
0.5083	28.05
0.5445	28.53
0.7428	31.80
0.7916	32.84
0.8362	33.77
0.9274	35.75

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methane, bromochloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0887	25.40
0.1583	25.52
0.2451	25.85
0.3372	26.35
0.4046	26.93
0.4370	27.22
0.4901	27.85
0.5083	28.05
0.5445	28.53
0.7428	31.80
0.7916	32.84
0.8362	33.77
0.9274	35.75

Mass density, kg/m3 [ref]

Fixed			Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Methane, bromochloro- (1) - Liquid	Mass density, kg/m3 - Liquid
101.33	288.15	0.0000	906.71
101.33	288.15	0.0961	976.08
101.33	288.15	0.2333	1083.23
101.33	288.15	0.3083	1145.77
101.33	288.15	0.4015	1228.4
101.33	288.15	0.5004	1322.97
101.33	288.15	0.6040	1430.45
101.33	288.15	0.7004	1538.94
101.33	288.15	0.7987	1659.96
101.33	288.15	0.9032	1800.66
101.33	288.15	1.0000	1945.94
101.33	298.15	0.0000	894.97
101.33	298.15	0.0961	963.62
101.33	298.15	0.2333	1069.74
101.33	298.15	0.3083	1131.77
101.33	298.15	0.4015	1213.84
101.33	298.15	0.5004	1308.02
101.33	298.15	0.6040	1414.77
101.33	298.15	0.7004	1522.14
101.33	298.15	0.7987	1641.51
101.33	298.15	0.9032	1780.71
101.33	298.15	1.0000	1924.88
101.33	308.15	0.0000	881.87
101.33	308.15	0.0961	949.99
101.33	308.15	0.2333	1054.79
101.33	308.15	0.3083	1116.41
101.33	308.15	0.4015	1197.33
101.33	308.15	0.5004	1290.38
101.33	308.15	0.6040	1396.09
101.33	308.15	0.7004	1502.46
101.33	308.15	0.7987	1620.66
101.33	308.15	0.9032	1758.33
101.33	308.15	1.0000	1900.86
200.00	298.15	0.2995	1118.5
200.00	298.15	0.5013	1299.53
200.00	298.15	0.6994	1514.36
600.00	298.15	0.2995	1119.03
600.00	298.15	0.5013	1300.17
700.00	298.15	0.6994	1515.04
1100.00	298.15	0.2995	1119.69
1200.00	298.15	0.5013	1300.97
1200.00	298.15	0.6994	1515.77
1900.00	298.15	0.6994	1516.63
2000.00	298.15	0.2995	1120.79
2100.00	298.15	0.5013	1301.96
3000.00	298.15	0.5013	1303.21
3100.00	298.15	0.2995	1121.97
3100.00	298.15	0.6994	1518.35
4000.00	298.15	0.2995	1123.04
4000.00	298.15	0.5013	1304.49
4000.00	298.15	0.6994	1519.64
4900.00	298.15	0.5013	1305.64
5100.00	298.15	0.2995	1124.32
5100.00	298.15	0.6994	1521.08
5800.00	298.15	0.6994	1522.03
6000.00	298.15	0.5013	1306.93
6100.00	298.15	0.2995	1125.53
6800.00	298.15	0.6994	1523.33
6900.00	298.15	0.2995	1126.38
7000.00	298.15	0.5013	1308.07
7800.00	298.15	0.5013	1309.22
7900.00	298.15	0.2995	1127.44
7900.00	298.15	0.6994	1524.7
8700.00	298.15	0.6994	1525.86
8800.00	298.15	0.5013	1310.44
9000.00	298.15	0.2995	1128.74
9800.00	298.15	0.5013	1311.74
9800.00	298.15	0.6994	1527.42
9900.00	298.15	0.2995	1129.86
11800.00	298.15	0.2995	1131.84
11900.00	298.15	0.6994	1530.29
12100.00	298.15	0.5013	1314.57
13800.00	298.15	0.2995	1134.16
13800.00	298.15	0.6994	1532.98
13900.00	298.15	0.5013	1316.83
15700.00	298.15	0.2995	1136.18
15900.00	298.15	0.5013	1319.23
15900.00	298.15	0.6994	1535.7
17600.00	298.15	0.5013	1321.38
17700.00	298.15	0.2995	1138.39
17700.00	298.15	0.6994	1538.2
19200.00	298.15	0.6994	1540.32
19400.00	298.15	0.6994	1540.59
19900.00	298.15	0.5013	1324.19
20000.00	298.15	0.2995	1140.92

Mass density, kg/m3 [ref]

Fixed			Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Methane, bromochloro- (1) - Liquid	Mass density, kg/m3 - Liquid
101.33	288.15	0.0000	906.71
101.33	288.15	0.0961	976.08
101.33	288.15	0.2333	1083.23
101.33	288.15	0.3083	1145.77
101.33	288.15	0.4015	1228.4
101.33	288.15	0.5004	1322.97
101.33	288.15	0.6040	1430.45
101.33	288.15	0.7004	1538.94
101.33	288.15	0.7987	1659.96
101.33	288.15	0.9032	1800.66
101.33	288.15	1.0000	1945.94
101.33	298.15	0.0000	894.97
101.33	298.15	0.0961	963.62
101.33	298.15	0.2333	1069.74
101.33	298.15	0.3083	1131.77
101.33	298.15	0.4015	1213.84
101.33	298.15	0.5004	1308.02
101.33	298.15	0.6040	1414.77
101.33	298.15	0.7004	1522.14
101.33	298.15	0.7987	1641.51
101.33	298.15	0.9032	1780.71
101.33	298.15	1.0000	1924.88
101.33	308.15	0.0000	881.87
101.33	308.15	0.0961	949.99
101.33	308.15	0.2333	1054.79
101.33	308.15	0.3083	1116.41
101.33	308.15	0.4015	1197.33
101.33	308.15	0.5004	1290.38
101.33	308.15	0.6040	1396.09
101.33	308.15	0.7004	1502.46
101.33	308.15	0.7987	1620.66
101.33	308.15	0.9032	1758.33
101.33	308.15	1.0000	1900.86
200.00	298.15	0.2995	1118.5
200.00	298.15	0.5013	1299.53
200.00	298.15	0.6994	1514.36
600.00	298.15	0.2995	1119.03
600.00	298.15	0.5013	1300.17
700.00	298.15	0.6994	1515.04
1100.00	298.15	0.2995	1119.69
1200.00	298.15	0.5013	1300.97
1200.00	298.15	0.6994	1515.77
1900.00	298.15	0.6994	1516.63
2000.00	298.15	0.2995	1120.79
2100.00	298.15	0.5013	1301.96
3000.00	298.15	0.5013	1303.21
3100.00	298.15	0.2995	1121.97
3100.00	298.15	0.6994	1518.35
4000.00	298.15	0.2995	1123.04
4000.00	298.15	0.5013	1304.49
4000.00	298.15	0.6994	1519.64
4900.00	298.15	0.5013	1305.64
5100.00	298.15	0.2995	1124.32
5100.00	298.15	0.6994	1521.08
5800.00	298.15	0.6994	1522.03
6000.00	298.15	0.5013	1306.93
6100.00	298.15	0.2995	1125.53
6800.00	298.15	0.6994	1523.33
6900.00	298.15	0.2995	1126.38
7000.00	298.15	0.5013	1308.07
7800.00	298.15	0.5013	1309.22
7900.00	298.15	0.2995	1127.44
7900.00	298.15	0.6994	1524.7
8700.00	298.15	0.6994	1525.86
8800.00	298.15	0.5013	1310.44
9000.00	298.15	0.2995	1128.74
9800.00	298.15	0.5013	1311.74
9800.00	298.15	0.6994	1527.42
9900.00	298.15	0.2995	1129.86
11800.00	298.15	0.2995	1131.84
11900.00	298.15	0.6994	1530.29
12100.00	298.15	0.5013	1314.57
13800.00	298.15	0.2995	1134.16
13800.00	298.15	0.6994	1532.98
13900.00	298.15	0.5013	1316.83
15700.00	298.15	0.2995	1136.18
15900.00	298.15	0.5013	1319.23
15900.00	298.15	0.6994	1535.7
17600.00	298.15	0.5013	1321.38
17700.00	298.15	0.2995	1138.39
17700.00	298.15	0.6994	1538.2
19200.00	298.15	0.6994	1540.32
19400.00	298.15	0.6994	1540.59
19900.00	298.15	0.5013	1324.19
20000.00	298.15	0.2995	1140.92

Sources

• Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
• Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 K