Mixture of Methane, dibromo- + Ethyl Acetate

Datasets

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

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

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methane, dibromo- (1) - Liquid	Mole fraction of Methane, dibromo- (1) - Gas
0.0710	0.0315
0.0936	0.0429
0.1817	0.0882
0.2469	0.1365
0.3738	0.2339
0.4147	0.2669
0.4929	0.3405
0.5222	0.3701
0.6137	0.4568
0.6855	0.5355
0.7001	0.5610
0.8084	0.6908
0.8306	0.7166
0.9154	0.8192

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Methane, dibromo- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0710	24.31
0.0936	23.95
0.1817	22.68
0.2469	21.75
0.3738	20.09
0.4147	19.52
0.4929	18.50
0.5222	18.09
0.6137	16.90
0.6855	16.05
0.7001	15.81
0.8084	14.69
0.8306	14.51
0.9154	13.73

Mass density, kg/m3 [ref]

Fixed			Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Methane, dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
101.33	288.15	0.0000	906.71
101.33	288.15	0.0522	966.58
101.33	288.15	0.2014	1147.77
101.33	288.15	0.3006	1277.79
101.33	288.15	0.4028	1419.89
101.33	288.15	0.4852	1542.09
101.33	288.15	0.6012	1725.96
101.33	288.15	0.7001	1895.61
101.33	288.15	0.8077	2095.3
101.33	288.15	0.8997	2281.45
101.33	288.15	1.0000	2501.88
101.33	298.15	0.0000	894.97
101.33	298.15	0.0522	954.36
101.33	298.15	0.2014	1133.83
101.33	298.15	0.3006	1262.61
101.33	298.15	0.4028	1404.06
101.33	298.15	0.4852	1525.0
101.33	298.15	0.6012	1707.9
101.33	298.15	0.7001	1876.1
101.33	298.15	0.8077	2074.59
101.33	298.15	0.8997	2259.57
101.33	298.15	1.0000	2478.37
101.33	308.15	0.0000	882.27
101.33	308.15	0.0522	940.97
101.33	308.15	0.2014	1118.5
101.33	308.15	0.3006	1245.98
101.33	308.15	0.4028	1385.7
101.33	308.15	0.4852	1505.67
101.33	308.15	0.6012	1686.98
101.33	308.15	0.7001	1854.24
101.33	308.15	0.8077	2050.67
101.33	308.15	0.8997	2234.29
101.33	308.15	1.0000	2451.74
200.00	298.15	0.2995	1260.2
200.00	298.15	0.5013	1549.45
200.00	298.15	0.6994	1874.05
500.00	298.15	0.2995	1260.63
600.00	298.15	0.5013	1550.03
600.00	298.15	0.6994	1874.73
1100.00	298.15	0.2995	1261.34
1100.00	298.15	0.5013	1550.84
1200.00	298.15	0.6994	1875.51
1900.00	298.15	0.5013	1551.83
2100.00	298.15	0.2995	1262.47
2200.00	298.15	0.6994	1876.85
2900.00	298.15	0.2995	1263.67
2900.00	298.15	0.5013	1553.29
2900.00	298.15	0.6994	1878.02
3700.00	298.15	0.2995	1264.58
3900.00	298.15	0.5013	1554.65
4200.00	298.15	0.6994	1879.75
4700.00	298.15	0.5013	1555.68
4800.00	298.15	0.2995	1265.79
5200.00	298.15	0.6994	1881.21
5900.00	298.15	0.2995	1267.24
6000.00	298.15	0.5013	1557.43
6000.00	298.15	0.6994	1882.25
6700.00	298.15	0.5013	1558.4
6800.00	298.15	0.2995	1268.29
7000.00	298.15	0.6994	1883.78
7900.00	298.15	0.5013	1560.0
8000.00	298.15	0.2995	1269.58
8100.00	298.15	0.6994	1885.33
8600.00	298.15	0.5013	1561.02
8900.00	298.15	0.2995	1270.84
9100.00	298.15	0.6994	1887.0
9800.00	298.15	0.2995	1271.89
10000.00	298.15	0.5013	1562.92
10000.00	298.15	0.6994	1888.23
10400.00	298.15	0.6994	1888.73
12000.00	298.15	0.5013	1565.67
12100.00	298.15	0.2995	1274.55
12300.00	298.15	0.6994	1891.62
13800.00	298.15	0.5013	1568.24
14000.00	298.15	0.2995	1276.89
14000.00	298.15	0.6994	1894.37
15800.00	298.15	0.2995	1278.96
15800.00	298.15	0.5013	1570.87
15900.00	298.15	0.6994	1897.08
17600.00	298.15	0.5013	1573.34
17800.00	298.15	0.6994	1900.02
17900.00	298.15	0.2995	1281.5
19800.00	298.15	0.5013	1576.4
19800.00	298.15	0.6994	1903.09
20100.00	298.15	0.2995	1284.19

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

Note: These property values are available through the Cheméo API. A free account gives you an access key.