Mixture of Carbon dioxide + Acetic acid, 2-ethylhexyl ester
Datasets
-
Pc - Critical pressure, kPa (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (2)
Critical pressure, kPa
[ref]
Mole fraction of Acetic acid, 2-ethylhexyl ester (2) - Liquid |
Critical pressure, kPa - Liquid |
0.0230 |
8190.00 |
0.0440 |
11590.00 |
0.0640 |
14480.00 |
0.0800 |
16580.00 |
0.0950 |
18240.00 |
Critical pressure, kPa
[ref]
Mole fraction of Acetic acid, 2-ethylhexyl ester (2) - Liquid |
Critical pressure, kPa - Liquid |
0.0230 |
8190.00 |
0.0440 |
11590.00 |
0.0640 |
14480.00 |
0.0800 |
16580.00 |
0.0950 |
18240.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Acetic acid, 2-ethylhexyl ester (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.20 |
0.0440 |
8140.00 |
313.20 |
0.0640 |
8080.00 |
313.20 |
0.0760 |
8010.00 |
313.20 |
0.0800 |
7920.00 |
313.20 |
0.0940 |
7830.00 |
313.20 |
0.0950 |
7810.00 |
313.20 |
0.1040 |
7730.00 |
313.20 |
0.1190 |
7700.00 |
313.20 |
0.1300 |
7610.00 |
313.20 |
0.1620 |
7220.00 |
313.20 |
0.1980 |
6790.00 |
313.20 |
0.2520 |
6240.00 |
313.20 |
0.2790 |
6100.00 |
313.20 |
0.2940 |
6080.00 |
313.20 |
0.3240 |
6030.00 |
313.20 |
0.3600 |
5830.00 |
313.20 |
0.4010 |
5130.00 |
313.20 |
0.4690 |
4720.00 |
313.20 |
0.4980 |
4420.00 |
333.20 |
0.0640 |
11590.00 |
333.20 |
0.0760 |
11350.00 |
333.20 |
0.0800 |
11310.00 |
333.20 |
0.0940 |
10950.00 |
333.20 |
0.0950 |
10910.00 |
333.20 |
0.1040 |
10890.00 |
333.20 |
0.1190 |
10750.00 |
333.20 |
0.1300 |
10680.00 |
333.20 |
0.1620 |
9950.00 |
333.20 |
0.1980 |
9170.00 |
333.20 |
0.2520 |
8500.00 |
333.20 |
0.2790 |
8060.00 |
333.20 |
0.2940 |
7930.00 |
333.20 |
0.3240 |
7840.00 |
333.20 |
0.3600 |
7310.00 |
333.20 |
0.4010 |
6410.00 |
333.20 |
0.4690 |
6030.00 |
333.20 |
0.4980 |
5460.00 |
353.20 |
0.0760 |
14470.00 |
353.20 |
0.0800 |
14410.00 |
353.20 |
0.0940 |
14380.00 |
353.20 |
0.0950 |
14310.00 |
353.20 |
0.1040 |
14140.00 |
353.20 |
0.1190 |
14060.00 |
353.20 |
0.1300 |
13810.00 |
353.20 |
0.1620 |
12810.00 |
353.20 |
0.1980 |
11900.00 |
353.20 |
0.2520 |
10680.00 |
353.20 |
0.2790 |
10160.00 |
353.20 |
0.2940 |
9690.00 |
353.20 |
0.3240 |
9560.00 |
353.20 |
0.3600 |
8970.00 |
353.20 |
0.4010 |
7950.00 |
353.20 |
0.4690 |
7140.00 |
353.20 |
0.4980 |
6590.00 |
373.20 |
0.0940 |
16540.00 |
373.20 |
0.0950 |
16590.00 |
373.20 |
0.1040 |
16460.00 |
373.20 |
0.1190 |
16240.00 |
373.20 |
0.1300 |
15930.00 |
373.20 |
0.1620 |
15360.00 |
373.20 |
0.1980 |
14310.00 |
373.20 |
0.2520 |
12590.00 |
373.20 |
0.2790 |
12030.00 |
373.20 |
0.2940 |
11710.00 |
373.20 |
0.3240 |
11260.00 |
373.20 |
0.3600 |
10380.00 |
373.20 |
0.4010 |
9220.00 |
373.20 |
0.4690 |
8040.00 |
373.20 |
0.4980 |
7520.00 |
393.20 |
0.1040 |
18100.00 |
393.20 |
0.1190 |
18000.00 |
393.20 |
0.1300 |
17820.00 |
393.20 |
0.1620 |
17430.00 |
393.20 |
0.1980 |
16450.00 |
393.20 |
0.2520 |
14730.00 |
393.20 |
0.2790 |
14160.00 |
393.20 |
0.2940 |
13690.00 |
393.20 |
0.3240 |
12840.00 |
393.20 |
0.3600 |
11760.00 |
393.20 |
0.4010 |
10520.00 |
393.20 |
0.4690 |
9000.00 |
393.20 |
0.4980 |
8390.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Acetic acid, 2-ethylhexyl ester (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
313.20 |
0.0440 |
8140.00 |
313.20 |
0.0640 |
8080.00 |
313.20 |
0.0760 |
8010.00 |
313.20 |
0.0800 |
7920.00 |
313.20 |
0.0940 |
7830.00 |
313.20 |
0.0950 |
7810.00 |
313.20 |
0.1040 |
7730.00 |
313.20 |
0.1190 |
7700.00 |
313.20 |
0.1300 |
7610.00 |
313.20 |
0.1620 |
7220.00 |
313.20 |
0.1980 |
6790.00 |
313.20 |
0.2520 |
6240.00 |
313.20 |
0.2790 |
6100.00 |
313.20 |
0.2940 |
6080.00 |
313.20 |
0.3240 |
6030.00 |
313.20 |
0.3600 |
5830.00 |
313.20 |
0.4010 |
5130.00 |
313.20 |
0.4690 |
4720.00 |
313.20 |
0.4980 |
4420.00 |
333.20 |
0.0640 |
11590.00 |
333.20 |
0.0760 |
11350.00 |
333.20 |
0.0800 |
11310.00 |
333.20 |
0.0940 |
10950.00 |
333.20 |
0.0950 |
10910.00 |
333.20 |
0.1040 |
10890.00 |
333.20 |
0.1190 |
10750.00 |
333.20 |
0.1300 |
10680.00 |
333.20 |
0.1620 |
9950.00 |
333.20 |
0.1980 |
9170.00 |
333.20 |
0.2520 |
8500.00 |
333.20 |
0.2790 |
8060.00 |
333.20 |
0.2940 |
7930.00 |
333.20 |
0.3240 |
7840.00 |
333.20 |
0.3600 |
7310.00 |
333.20 |
0.4010 |
6410.00 |
333.20 |
0.4690 |
6030.00 |
333.20 |
0.4980 |
5460.00 |
353.20 |
0.0760 |
14470.00 |
353.20 |
0.0800 |
14410.00 |
353.20 |
0.0940 |
14380.00 |
353.20 |
0.0950 |
14310.00 |
353.20 |
0.1040 |
14140.00 |
353.20 |
0.1190 |
14060.00 |
353.20 |
0.1300 |
13810.00 |
353.20 |
0.1620 |
12810.00 |
353.20 |
0.1980 |
11900.00 |
353.20 |
0.2520 |
10680.00 |
353.20 |
0.2790 |
10160.00 |
353.20 |
0.2940 |
9690.00 |
353.20 |
0.3240 |
9560.00 |
353.20 |
0.3600 |
8970.00 |
353.20 |
0.4010 |
7950.00 |
353.20 |
0.4690 |
7140.00 |
353.20 |
0.4980 |
6590.00 |
373.20 |
0.0940 |
16540.00 |
373.20 |
0.0950 |
16590.00 |
373.20 |
0.1040 |
16460.00 |
373.20 |
0.1190 |
16240.00 |
373.20 |
0.1300 |
15930.00 |
373.20 |
0.1620 |
15360.00 |
373.20 |
0.1980 |
14310.00 |
373.20 |
0.2520 |
12590.00 |
373.20 |
0.2790 |
12030.00 |
373.20 |
0.2940 |
11710.00 |
373.20 |
0.3240 |
11260.00 |
373.20 |
0.3600 |
10380.00 |
373.20 |
0.4010 |
9220.00 |
373.20 |
0.4690 |
8040.00 |
373.20 |
0.4980 |
7520.00 |
393.20 |
0.1040 |
18100.00 |
393.20 |
0.1190 |
18000.00 |
393.20 |
0.1300 |
17820.00 |
393.20 |
0.1620 |
17430.00 |
393.20 |
0.1980 |
16450.00 |
393.20 |
0.2520 |
14730.00 |
393.20 |
0.2790 |
14160.00 |
393.20 |
0.2940 |
13690.00 |
393.20 |
0.3240 |
12840.00 |
393.20 |
0.3600 |
11760.00 |
393.20 |
0.4010 |
10520.00 |
393.20 |
0.4690 |
9000.00 |
393.20 |
0.4980 |
8390.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Acetic acid, 2-ethylhexyl ester (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
333.20 |
0.0230 |
11450.00 |
353.20 |
0.0230 |
14000.00 |
353.20 |
0.0440 |
14260.00 |
373.20 |
0.0230 |
15370.00 |
373.20 |
0.0440 |
16200.00 |
373.20 |
0.0640 |
16410.00 |
373.20 |
0.0760 |
16520.00 |
393.20 |
0.0230 |
15310.00 |
393.20 |
0.0440 |
17030.00 |
393.20 |
0.0640 |
17840.00 |
393.20 |
0.0760 |
18070.00 |
393.20 |
0.0800 |
18110.00 |
393.20 |
0.0940 |
18230.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Acetic acid, 2-ethylhexyl ester (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
333.20 |
0.0230 |
11450.00 |
353.20 |
0.0230 |
14000.00 |
353.20 |
0.0440 |
14260.00 |
373.20 |
0.0230 |
15370.00 |
373.20 |
0.0440 |
16200.00 |
373.20 |
0.0640 |
16410.00 |
373.20 |
0.0760 |
16520.00 |
393.20 |
0.0230 |
15310.00 |
393.20 |
0.0440 |
17030.00 |
393.20 |
0.0640 |
17840.00 |
393.20 |
0.0760 |
18070.00 |
393.20 |
0.0800 |
18110.00 |
393.20 |
0.0940 |
18230.00 |
Sources