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. 2013 May 12;2013:408491. doi: 10.1155/2013/408491

Table 1.

SFE operational conditions tested.

Assay T (°C) Time (min) CO2 flow (g min−1) Pressure (bar) Modifier Modifier (%) Modifier flow (mL min−1) Fractions obtained
None None None A100, A120, A140, A160, A200, A250, A300
1 40 30 —* 100, 120, 140, 160, 200, 250, 300 Ethanol —* 0.1 B100, B120, B140, B160, B200, B250, B300
—* 0.2 C100, C120, C140, C160, C200, C250, C300

2 40 30 3 100, 120, 140, 160, 200, 250, 300 Ethanol 3
6
0.1
0.2
D100, D120, D140, D160, D200, D250, D300  
E100, E120, E140, E160, E200, E250, E300

3 40 30 3 140 Ethanol
Methanol
0, 0.5, 1, 1.5, 2, 2.5, 3 0.0, 0.02, 0.03, 0.05, 0.06, 0.08, 0.1 F0, F0.5, F1, F1.5, F2, F2.5, F3  
G0, G0.5, G1, G1.5, G2, G2.5, G3

*In pressure mode, neither CO2 flow nor modifier percentage were controlled.

HHS Vulnerability Disclosure