Mixture of Carbon dioxide + Ethanol + Tridecane
Datasets
-
γ - Surface tension liquid-gas, N/m (2)
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (2) - Gas |
Surface tension liquid-gas, N/m - Liquid |
333.15 |
6020.00 |
0.0202 |
0.0097 |
333.15 |
7080.00 |
0.0200 |
0.0080 |
333.15 |
8030.00 |
0.0201 |
0.0058 |
333.15 |
8970.00 |
0.0202 |
0.0042 |
333.15 |
10000.00 |
0.0202 |
0.0023 |
333.15 |
9930.00 |
0.0412 |
0.0017 |
353.15 |
7630.00 |
0.0211 |
0.0084 |
353.15 |
8760.00 |
0.0214 |
0.0069 |
353.15 |
10170.00 |
0.0209 |
0.0049 |
353.15 |
11090.00 |
0.0200 |
0.0038 |
353.15 |
11860.00 |
0.0204 |
0.0029 |
353.15 |
10050.00 |
0.0402 |
0.0043 |
353.15 |
10990.00 |
0.0406 |
0.0034 |
353.15 |
11900.00 |
0.0408 |
0.0022 |
373.15 |
7950.00 |
0.0225 |
0.0088 |
373.15 |
9420.00 |
0.0224 |
0.0070 |
373.15 |
11320.00 |
0.0214 |
0.0050 |
373.15 |
12520.00 |
0.0204 |
0.0037 |
373.15 |
13640.00 |
0.0206 |
0.0029 |
373.15 |
9100.00 |
0.0401 |
0.0067 |
373.15 |
10100.00 |
0.0405 |
0.0057 |
373.15 |
11260.00 |
0.0408 |
0.0045 |
373.15 |
12460.00 |
0.0412 |
0.0035 |
373.15 |
13770.00 |
0.0409 |
0.0023 |
373.15 |
9000.00 |
0.0610 |
0.0063 |
373.15 |
10000.00 |
0.0610 |
0.0052 |
373.15 |
11060.00 |
0.0608 |
0.0043 |
373.15 |
11990.00 |
0.0615 |
0.0032 |
373.15 |
12980.00 |
0.0616 |
0.0024 |
373.15 |
9960.00 |
0.0823 |
0.0046 |
373.15 |
11040.00 |
0.0817 |
0.0037 |
373.15 |
12040.00 |
0.0821 |
0.0025 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (2) - Gas |
Surface tension liquid-gas, N/m - Liquid |
333.15 |
6020.00 |
0.0202 |
0.0097 |
333.15 |
7080.00 |
0.0200 |
0.0080 |
333.15 |
8030.00 |
0.0201 |
0.0058 |
333.15 |
8970.00 |
0.0202 |
0.0042 |
333.15 |
10000.00 |
0.0202 |
0.0023 |
333.15 |
9930.00 |
0.0412 |
0.0017 |
353.15 |
7630.00 |
0.0211 |
0.0084 |
353.15 |
8760.00 |
0.0214 |
0.0069 |
353.15 |
10170.00 |
0.0209 |
0.0049 |
353.15 |
11090.00 |
0.0200 |
0.0038 |
353.15 |
11860.00 |
0.0204 |
0.0029 |
353.15 |
10050.00 |
0.0402 |
0.0043 |
353.15 |
10990.00 |
0.0406 |
0.0034 |
353.15 |
11900.00 |
0.0408 |
0.0022 |
373.15 |
7950.00 |
0.0225 |
0.0088 |
373.15 |
9420.00 |
0.0224 |
0.0070 |
373.15 |
11320.00 |
0.0214 |
0.0050 |
373.15 |
12520.00 |
0.0204 |
0.0037 |
373.15 |
13640.00 |
0.0206 |
0.0029 |
373.15 |
9100.00 |
0.0401 |
0.0067 |
373.15 |
10100.00 |
0.0405 |
0.0057 |
373.15 |
11260.00 |
0.0408 |
0.0045 |
373.15 |
12460.00 |
0.0412 |
0.0035 |
373.15 |
13770.00 |
0.0409 |
0.0023 |
373.15 |
9000.00 |
0.0610 |
0.0063 |
373.15 |
10000.00 |
0.0610 |
0.0052 |
373.15 |
11060.00 |
0.0608 |
0.0043 |
373.15 |
11990.00 |
0.0615 |
0.0032 |
373.15 |
12980.00 |
0.0616 |
0.0024 |
373.15 |
9960.00 |
0.0823 |
0.0046 |
373.15 |
11040.00 |
0.0817 |
0.0037 |
373.15 |
12040.00 |
0.0821 |
0.0025 |
Sources