Mixture of Ethyl Acetate + Ethane, 1-bromo-2-chloro-

Datasets

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

Mole fraction of Ethane, 1-bromo-2-chloro- (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Ethane, 1-bromo-2-chloro- (2) - Liquid	Mole fraction of Ethane, 1-bromo-2-chloro- (2) - Gas
0.0879	0.0344
0.1691	0.0749
0.2861	0.1377
0.4053	0.2006
0.4305	0.2187
0.4676	0.2595
0.5236	0.2954
0.5716	0.3470
0.6032	0.3733
0.6367	0.4012
0.7260	0.5158
0.7487	0.5372
0.7691	0.5657
0.8086	0.6225
0.8449	0.6823
0.8784	0.7387
0.9144	0.8074

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Ethane, 1-bromo-2-chloro- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0879	23.78
0.1691	22.37
0.2861	20.40
0.4053	18.23
0.4305	17.72
0.4676	17.10
0.5236	16.07
0.5716	15.27
0.6032	14.78
0.6367	14.25
0.7260	12.89
0.7487	12.59
0.7691	12.31
0.8086	11.71
0.8449	11.18
0.8784	10.68
0.9144	10.16

Mass density, kg/m3 [ref]

Fixed			Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, 1-bromo-2-chloro- (2) - Liquid	Mass density, kg/m3 - Liquid
101.33	288.15	0.0000	906.71
101.33	288.15	0.1080	984.97
101.33	288.15	0.1985	1051.71
101.33	288.15	0.2997	1128.56
101.33	288.15	0.3988	1205.99
101.33	288.15	0.5008	1288.67
101.33	288.15	0.5477	1327.76
101.33	288.15	0.6462	1412.26
101.33	288.15	0.7653	1518.63
101.33	288.15	0.8030	1553.45
101.33	288.15	0.9050	1650.02
101.33	288.15	1.0000	1744.36
101.33	298.15	0.0000	894.97
101.33	298.15	0.1080	972.55
101.33	298.15	0.1985	1039.06
101.33	298.15	0.2997	1115.49
101.33	298.15	0.3988	1192.41
101.33	298.15	0.5008	1274.57
101.33	298.15	0.5477	1313.32
101.33	298.15	0.6462	1397.28
101.33	298.15	0.7653	1503.13
101.33	298.15	0.8030	1537.71
101.33	298.15	0.9050	1634.03
101.33	298.15	1.0000	1727.88
101.33	308.15	0.0000	882.27
101.33	308.15	0.1080	959.03
101.33	308.15	0.1985	1024.94
101.33	308.15	0.2997	1100.59
101.33	308.15	0.3988	1177.02
101.33	308.15	0.5008	1258.55
101.33	308.15	0.5477	1296.96
101.33	308.15	0.6462	1380.36
101.33	308.15	0.7653	1485.56
101.33	308.15	0.8030	1519.81
101.33	308.15	0.9050	1615.55
101.33	308.15	1.0000	1708.86
200.00	298.15	0.2995	1115.91
200.00	298.15	0.5013	1278.27
200.00	298.15	0.6994	1442.43
500.00	298.15	0.2995	1116.35
600.00	298.15	0.6994	1443.12
700.00	298.15	0.5013	1278.85
1100.00	298.15	0.6994	1443.6
1200.00	298.15	0.2995	1117.05
1200.00	298.15	0.5013	1279.48
2100.00	298.15	0.2995	1118.11
2100.00	298.15	0.5013	1280.34
2100.00	298.15	0.6994	1444.65
2900.00	298.15	0.6994	1445.74
3000.00	298.15	0.2995	1119.13
3000.00	298.15	0.5013	1281.5
4000.00	298.15	0.2995	1120.19
4000.00	298.15	0.5013	1282.56
4100.00	298.15	0.6994	1447.07
5000.00	298.15	0.2995	1121.32
5000.00	298.15	0.5013	1283.71
5100.00	298.15	0.6994	1448.15
5800.00	298.15	0.2995	1122.17
5800.00	298.15	0.6994	1448.98
5900.00	298.15	0.5013	1284.8
7000.00	298.15	0.5013	1285.84
7000.00	298.15	0.6994	1450.32
7100.00	298.15	0.2995	1123.21
7700.00	298.15	0.6994	1451.09
7900.00	298.15	0.2995	1124.37
8000.00	298.15	0.5013	1286.92
8600.00	298.15	0.2995	1125.17
8700.00	298.15	0.5013	1287.86
8800.00	298.15	0.6994	1452.5
10100.00	298.15	0.2995	1126.71
10100.00	298.15	0.5013	1289.28
10300.00	298.15	0.6994	1454.22
11700.00	298.15	0.2995	1128.38
12000.00	298.15	0.5013	1291.48
12000.00	298.15	0.6994	1456.29
13700.00	298.15	0.5013	1293.44
13800.00	298.15	0.2995	1130.67
14000.00	298.15	0.6994	1458.57
15500.00	298.15	0.5013	1295.42
15900.00	298.15	0.2995	1132.71
15900.00	298.15	0.6994	1460.86
17400.00	298.15	0.6994	1462.58
17700.00	298.15	0.2995	1134.48
17900.00	298.15	0.5013	1298.2
19200.00	298.15	0.6994	1464.86
19700.00	298.15	0.2995	1136.76
19800.00	298.15	0.5013	1300.25

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.