Mixture of Carbon dioxide + Ethanol + Pentadecane
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 |
5960.00 |
0.0202 |
0.0105 |
333.15 |
7000.00 |
0.0202 |
0.0084 |
333.15 |
8020.00 |
0.0200 |
0.0066 |
333.15 |
8960.00 |
0.0203 |
0.0049 |
333.15 |
10060.00 |
0.0201 |
0.0032 |
333.15 |
9930.00 |
0.0412 |
0.0025 |
353.15 |
7200.00 |
0.0226 |
0.0098 |
353.15 |
7930.00 |
0.0203 |
0.0088 |
353.15 |
8830.00 |
0.0210 |
0.0077 |
353.15 |
10280.00 |
0.0207 |
0.0058 |
353.15 |
10960.00 |
0.0201 |
0.0049 |
353.15 |
11980.00 |
0.0202 |
0.0039 |
353.15 |
10000.00 |
0.0406 |
0.0051 |
353.15 |
11020.00 |
0.0404 |
0.0040 |
353.15 |
11890.00 |
0.0409 |
0.0032 |
353.15 |
12000.00 |
0.0613 |
0.0024 |
373.15 |
7430.00 |
0.0245 |
0.0102 |
373.15 |
8470.00 |
0.0213 |
0.0090 |
373.15 |
9580.00 |
0.0218 |
0.0079 |
373.15 |
10410.00 |
0.0205 |
0.0071 |
373.15 |
11500.00 |
0.0211 |
0.0059 |
373.15 |
12390.00 |
0.0205 |
0.0050 |
373.15 |
13510.00 |
0.0201 |
0.0040 |
373.15 |
9000.00 |
0.0406 |
0.0078 |
373.15 |
10060.00 |
0.0400 |
0.0067 |
373.15 |
11200.00 |
0.0411 |
0.0056 |
373.15 |
12460.00 |
0.0411 |
0.0044 |
373.15 |
13770.00 |
0.0409 |
0.0033 |
373.15 |
10040.00 |
0.0606 |
0.0060 |
373.15 |
11060.00 |
0.0606 |
0.0051 |
373.15 |
12000.00 |
0.0613 |
0.0042 |
373.15 |
12990.00 |
0.0614 |
0.0033 |
373.15 |
14030.00 |
0.0608 |
0.0025 |
373.15 |
8990.00 |
0.0814 |
0.0066 |
373.15 |
9970.00 |
0.0820 |
0.0056 |
373.15 |
10970.00 |
0.0822 |
0.0047 |
373.15 |
11800.00 |
0.0827 |
0.0038 |
373.15 |
13000.00 |
0.0826 |
0.0028 |
373.15 |
13970.00 |
0.0833 |
0.0019 |
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 |
5960.00 |
0.0202 |
0.0105 |
333.15 |
7000.00 |
0.0202 |
0.0084 |
333.15 |
8020.00 |
0.0200 |
0.0066 |
333.15 |
8960.00 |
0.0203 |
0.0049 |
333.15 |
10060.00 |
0.0201 |
0.0032 |
333.15 |
9930.00 |
0.0412 |
0.0025 |
353.15 |
7200.00 |
0.0226 |
0.0098 |
353.15 |
7930.00 |
0.0203 |
0.0088 |
353.15 |
8830.00 |
0.0210 |
0.0077 |
353.15 |
10280.00 |
0.0207 |
0.0058 |
353.15 |
10960.00 |
0.0201 |
0.0049 |
353.15 |
11980.00 |
0.0202 |
0.0039 |
353.15 |
10000.00 |
0.0406 |
0.0051 |
353.15 |
11020.00 |
0.0404 |
0.0040 |
353.15 |
11890.00 |
0.0409 |
0.0032 |
353.15 |
12000.00 |
0.0613 |
0.0024 |
373.15 |
7430.00 |
0.0245 |
0.0102 |
373.15 |
8470.00 |
0.0213 |
0.0090 |
373.15 |
9580.00 |
0.0218 |
0.0079 |
373.15 |
10410.00 |
0.0205 |
0.0071 |
373.15 |
11500.00 |
0.0211 |
0.0059 |
373.15 |
12390.00 |
0.0205 |
0.0050 |
373.15 |
13510.00 |
0.0201 |
0.0040 |
373.15 |
9000.00 |
0.0406 |
0.0078 |
373.15 |
10060.00 |
0.0400 |
0.0067 |
373.15 |
11200.00 |
0.0411 |
0.0056 |
373.15 |
12460.00 |
0.0411 |
0.0044 |
373.15 |
13770.00 |
0.0409 |
0.0033 |
373.15 |
10040.00 |
0.0606 |
0.0060 |
373.15 |
11060.00 |
0.0606 |
0.0051 |
373.15 |
12000.00 |
0.0613 |
0.0042 |
373.15 |
12990.00 |
0.0614 |
0.0033 |
373.15 |
14030.00 |
0.0608 |
0.0025 |
373.15 |
8990.00 |
0.0814 |
0.0066 |
373.15 |
9970.00 |
0.0820 |
0.0056 |
373.15 |
10970.00 |
0.0822 |
0.0047 |
373.15 |
11800.00 |
0.0827 |
0.0038 |
373.15 |
13000.00 |
0.0826 |
0.0028 |
373.15 |
13970.00 |
0.0833 |
0.0019 |
Sources