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

Excel

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6

Ethane, 1-bromo-2-chloro-

Name
Ethane, 1-bromo-2-chloro-
InChI
InChI=1S/C2H4BrCl/c3-1-2-4/h1-2H2
InChI Key
IBYHHJPAARCAIE-UHFFFAOYSA-N
Formula
C2H4BrCl
SMILES
ClCCBr
Mol. Weight (g/mol)
143.41
CAS
107-04-0
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Datasets

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

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

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

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

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