Mixture of Carbon dioxide + 9,12-Octadecadienoic acid (Z,Z)- + Ethanol
Datasets
-
Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Ethanol (3) - Liquid |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.5730 |
0.1433 |
303.00 |
6040.00 |
0.5730 |
0.1433 |
313.00 |
7320.00 |
0.5730 |
0.1433 |
323.00 |
8440.00 |
0.5730 |
0.1433 |
333.00 |
9560.00 |
0.5730 |
0.1433 |
343.00 |
10780.00 |
0.6058 |
0.1514 |
303.00 |
6760.00 |
0.6058 |
0.1514 |
313.00 |
8010.00 |
0.6058 |
0.1514 |
323.00 |
9430.00 |
0.6058 |
0.1514 |
333.00 |
10790.00 |
0.6058 |
0.1514 |
343.00 |
12170.00 |
0.6426 |
0.1606 |
303.00 |
7120.00 |
0.6426 |
0.1606 |
313.00 |
8750.00 |
0.6426 |
0.1606 |
323.00 |
10680.00 |
0.6426 |
0.1606 |
333.00 |
12850.00 |
0.6426 |
0.1606 |
343.00 |
14560.00 |
0.6578 |
0.1645 |
303.00 |
7010.00 |
0.6578 |
0.1645 |
313.00 |
8160.00 |
0.6578 |
0.1645 |
323.00 |
9760.00 |
0.6578 |
0.1645 |
333.00 |
11490.00 |
0.6578 |
0.1645 |
343.00 |
13350.00 |
0.6827 |
0.1707 |
303.00 |
7520.00 |
0.6827 |
0.1707 |
313.00 |
9230.00 |
0.6827 |
0.1707 |
323.00 |
11340.00 |
0.6827 |
0.1707 |
333.00 |
13430.00 |
0.6827 |
0.1707 |
343.00 |
15750.00 |
0.7046 |
0.1762 |
303.00 |
7910.00 |
0.7046 |
0.1762 |
313.00 |
10280.00 |
0.7046 |
0.1762 |
323.00 |
12310.00 |
0.7046 |
0.1762 |
333.00 |
14430.00 |
0.7046 |
0.1762 |
343.00 |
16440.00 |
0.7178 |
0.1795 |
303.00 |
8560.00 |
0.7178 |
0.1795 |
313.00 |
11030.00 |
0.7178 |
0.1795 |
323.00 |
13080.00 |
0.7178 |
0.1795 |
333.00 |
15190.00 |
0.7178 |
0.1795 |
343.00 |
17110.00 |
0.7408 |
0.1852 |
303.00 |
9380.00 |
0.7408 |
0.1852 |
313.00 |
11710.00 |
0.7408 |
0.1852 |
323.00 |
14110.00 |
0.7408 |
0.1852 |
333.00 |
16100.00 |
0.7408 |
0.1852 |
343.00 |
18170.00 |
0.7607 |
0.1902 |
303.00 |
9740.00 |
0.7607 |
0.1902 |
313.00 |
11880.00 |
0.7607 |
0.1902 |
323.00 |
14130.00 |
0.7607 |
0.1902 |
333.00 |
16240.00 |
0.7607 |
0.1902 |
343.00 |
18110.00 |
0.7801 |
0.1950 |
303.00 |
7960.00 |
0.7801 |
0.1950 |
313.00 |
10440.00 |
0.7801 |
0.1950 |
323.00 |
12600.00 |
0.7801 |
0.1950 |
333.00 |
14870.00 |
0.7801 |
0.1950 |
343.00 |
16660.00 |
0.7918 |
0.1980 |
303.00 |
6640.00 |
0.7918 |
0.1980 |
313.00 |
8220.00 |
0.7918 |
0.1980 |
323.00 |
9850.00 |
0.7918 |
0.1980 |
333.00 |
11610.00 |
0.7918 |
0.1980 |
343.00 |
13270.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Mole fraction of Ethanol (3) - Liquid |
Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
0.5730 |
0.1433 |
303.00 |
6040.00 |
0.5730 |
0.1433 |
313.00 |
7320.00 |
0.5730 |
0.1433 |
323.00 |
8440.00 |
0.5730 |
0.1433 |
333.00 |
9560.00 |
0.5730 |
0.1433 |
343.00 |
10780.00 |
0.6058 |
0.1514 |
303.00 |
6760.00 |
0.6058 |
0.1514 |
313.00 |
8010.00 |
0.6058 |
0.1514 |
323.00 |
9430.00 |
0.6058 |
0.1514 |
333.00 |
10790.00 |
0.6058 |
0.1514 |
343.00 |
12170.00 |
0.6426 |
0.1606 |
303.00 |
7120.00 |
0.6426 |
0.1606 |
313.00 |
8750.00 |
0.6426 |
0.1606 |
323.00 |
10680.00 |
0.6426 |
0.1606 |
333.00 |
12850.00 |
0.6426 |
0.1606 |
343.00 |
14560.00 |
0.6578 |
0.1645 |
303.00 |
7010.00 |
0.6578 |
0.1645 |
313.00 |
8160.00 |
0.6578 |
0.1645 |
323.00 |
9760.00 |
0.6578 |
0.1645 |
333.00 |
11490.00 |
0.6578 |
0.1645 |
343.00 |
13350.00 |
0.6827 |
0.1707 |
303.00 |
7520.00 |
0.6827 |
0.1707 |
313.00 |
9230.00 |
0.6827 |
0.1707 |
323.00 |
11340.00 |
0.6827 |
0.1707 |
333.00 |
13430.00 |
0.6827 |
0.1707 |
343.00 |
15750.00 |
0.7046 |
0.1762 |
303.00 |
7910.00 |
0.7046 |
0.1762 |
313.00 |
10280.00 |
0.7046 |
0.1762 |
323.00 |
12310.00 |
0.7046 |
0.1762 |
333.00 |
14430.00 |
0.7046 |
0.1762 |
343.00 |
16440.00 |
0.7178 |
0.1795 |
303.00 |
8560.00 |
0.7178 |
0.1795 |
313.00 |
11030.00 |
0.7178 |
0.1795 |
323.00 |
13080.00 |
0.7178 |
0.1795 |
333.00 |
15190.00 |
0.7178 |
0.1795 |
343.00 |
17110.00 |
0.7408 |
0.1852 |
303.00 |
9380.00 |
0.7408 |
0.1852 |
313.00 |
11710.00 |
0.7408 |
0.1852 |
323.00 |
14110.00 |
0.7408 |
0.1852 |
333.00 |
16100.00 |
0.7408 |
0.1852 |
343.00 |
18170.00 |
0.7607 |
0.1902 |
303.00 |
9740.00 |
0.7607 |
0.1902 |
313.00 |
11880.00 |
0.7607 |
0.1902 |
323.00 |
14130.00 |
0.7607 |
0.1902 |
333.00 |
16240.00 |
0.7607 |
0.1902 |
343.00 |
18110.00 |
0.7801 |
0.1950 |
303.00 |
7960.00 |
0.7801 |
0.1950 |
313.00 |
10440.00 |
0.7801 |
0.1950 |
323.00 |
12600.00 |
0.7801 |
0.1950 |
333.00 |
14870.00 |
0.7801 |
0.1950 |
343.00 |
16660.00 |
0.7918 |
0.1980 |
303.00 |
6640.00 |
0.7918 |
0.1980 |
313.00 |
8220.00 |
0.7918 |
0.1980 |
323.00 |
9850.00 |
0.7918 |
0.1980 |
333.00 |
11610.00 |
0.7918 |
0.1980 |
343.00 |
13270.00 |
Sources