Mixture of Heptadecane + Carbon dioxide + Ethanol
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 (3) - Gas |
Surface tension liquid-gas, N/m - Liquid |
333.15 |
6000.00 |
0.0199 |
0.0109 |
333.15 |
7030.00 |
0.0200 |
0.0090 |
333.15 |
7890.00 |
0.0203 |
0.0075 |
333.15 |
9000.00 |
0.0201 |
0.0055 |
333.15 |
10000.00 |
0.0201 |
0.0041 |
333.15 |
10030.00 |
0.0410 |
0.0028 |
353.15 |
8740.00 |
0.0194 |
0.0083 |
353.15 |
9490.00 |
0.0201 |
0.0074 |
353.15 |
10260.00 |
0.0207 |
0.0064 |
353.15 |
11880.00 |
0.0203 |
0.0047 |
353.15 |
12610.00 |
0.0198 |
0.0040 |
353.15 |
10000.00 |
0.0405 |
0.0059 |
353.15 |
11050.00 |
0.0400 |
0.0048 |
353.15 |
12000.00 |
0.0410 |
0.0036 |
353.15 |
12000.00 |
0.0614 |
0.0030 |
373.15 |
9260.00 |
0.0225 |
0.0090 |
373.15 |
9460.00 |
0.0201 |
0.0087 |
373.15 |
10490.00 |
0.0205 |
0.0076 |
373.15 |
10920.00 |
0.0195 |
0.0073 |
373.15 |
11460.00 |
0.0212 |
0.0068 |
373.15 |
12820.00 |
0.0193 |
0.0054 |
373.15 |
13620.00 |
0.0206 |
0.0049 |
373.15 |
14600.00 |
0.0201 |
0.0040 |
373.15 |
10150.00 |
0.0396 |
0.0076 |
373.15 |
11180.00 |
0.0411 |
0.0065 |
373.15 |
12600.00 |
0.0403 |
0.0051 |
373.15 |
12970.00 |
0.0407 |
0.0047 |
373.15 |
13910.00 |
0.0411 |
0.0040 |
373.15 |
10060.00 |
0.0604 |
0.0069 |
373.15 |
11060.00 |
0.0605 |
0.0058 |
373.15 |
11930.00 |
0.0616 |
0.0050 |
373.15 |
13020.00 |
0.0612 |
0.0042 |
373.15 |
14030.00 |
0.0608 |
0.0033 |
373.15 |
9990.00 |
0.0820 |
0.0058 |
373.15 |
10980.00 |
0.0822 |
0.0048 |
373.15 |
12060.00 |
0.0817 |
0.0041 |
373.15 |
13090.00 |
0.0819 |
0.0033 |
373.15 |
13900.00 |
0.0835 |
0.0026 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (3) - Gas |
Surface tension liquid-gas, N/m - Liquid |
333.15 |
6000.00 |
0.0199 |
0.0109 |
333.15 |
7030.00 |
0.0200 |
0.0090 |
333.15 |
7890.00 |
0.0203 |
0.0075 |
333.15 |
9000.00 |
0.0201 |
0.0055 |
333.15 |
10000.00 |
0.0201 |
0.0041 |
333.15 |
10030.00 |
0.0410 |
0.0028 |
353.15 |
8740.00 |
0.0194 |
0.0083 |
353.15 |
9490.00 |
0.0201 |
0.0074 |
353.15 |
10260.00 |
0.0207 |
0.0064 |
353.15 |
11880.00 |
0.0203 |
0.0047 |
353.15 |
12610.00 |
0.0198 |
0.0040 |
353.15 |
10000.00 |
0.0405 |
0.0059 |
353.15 |
11050.00 |
0.0400 |
0.0048 |
353.15 |
12000.00 |
0.0410 |
0.0036 |
353.15 |
12000.00 |
0.0614 |
0.0030 |
373.15 |
9260.00 |
0.0225 |
0.0090 |
373.15 |
9460.00 |
0.0201 |
0.0087 |
373.15 |
10490.00 |
0.0205 |
0.0076 |
373.15 |
10920.00 |
0.0195 |
0.0073 |
373.15 |
11460.00 |
0.0212 |
0.0068 |
373.15 |
12820.00 |
0.0193 |
0.0054 |
373.15 |
13620.00 |
0.0206 |
0.0049 |
373.15 |
14600.00 |
0.0201 |
0.0040 |
373.15 |
10150.00 |
0.0396 |
0.0076 |
373.15 |
11180.00 |
0.0411 |
0.0065 |
373.15 |
12600.00 |
0.0403 |
0.0051 |
373.15 |
12970.00 |
0.0407 |
0.0047 |
373.15 |
13910.00 |
0.0411 |
0.0040 |
373.15 |
10060.00 |
0.0604 |
0.0069 |
373.15 |
11060.00 |
0.0605 |
0.0058 |
373.15 |
11930.00 |
0.0616 |
0.0050 |
373.15 |
13020.00 |
0.0612 |
0.0042 |
373.15 |
14030.00 |
0.0608 |
0.0033 |
373.15 |
9990.00 |
0.0820 |
0.0058 |
373.15 |
10980.00 |
0.0822 |
0.0048 |
373.15 |
12060.00 |
0.0817 |
0.0041 |
373.15 |
13090.00 |
0.0819 |
0.0033 |
373.15 |
13900.00 |
0.0835 |
0.0026 |
Sources