Mixture of Methane, dibromo- + Ethyl Acetate

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Methane, dibromo-

Name
Methane, dibromo-
InChI
InChI=1S/CH2Br2/c2-1-3/h1H2
InChI Key
FJBFPHVGVWTDIP-UHFFFAOYSA-N
Formula
CH2Br2
SMILES
BrCBr
Mol. Weight (g/mol)
173.84
CAS
74-95-3

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
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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 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

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

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

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