Effect of microalga preconditioning on supercritical CO2 ... - ISSF 2012
Effect of microalga preconditioning on supercritical CO2 ... - ISSF 2012
Effect of microalga preconditioning on supercritical CO2 ... - ISSF 2012
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y (mg astaxantina/gr <str<strong>on</strong>g>microalga</str<strong>on</strong>g>)<br />
12<br />
10<br />
8<br />
6<br />
4<br />
2<br />
550, 70<br />
450, 70<br />
350,70<br />
550, 40<br />
450,40<br />
350, 40<br />
0<br />
0 1 2 3 4 5 6<br />
F (kg de <strong>CO2</strong>/ g <str<strong>on</strong>g>microalga</str<strong>on</strong>g>)<br />
Figure 2. Cumulative extracti<strong>on</strong> curves <str<strong>on</strong>g>of</str<strong>on</strong>g> aqueous Haematococcus pluvialis homogenate samples as a functi<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> extracti<strong>on</strong><br />
temperature and pressure.<br />
effect <str<strong>on</strong>g>of</str<strong>on</strong>g> the water layer that is not very soluble in sc<strong>CO2</strong> and may retard extracti<strong>on</strong>. Water is extracted, however,<br />
and its removal can explain the subsequent increase in extracti<strong>on</strong> rate following the initial lag period. Dry<br />
pockets may have developed during extracti<strong>on</strong> that exposed H. pluvialis to sc<strong>CO2</strong> and facilitated removal <str<strong>on</strong>g>of</str<strong>on</strong>g><br />
astaxanthin and other comp<strong>on</strong>ents <str<strong>on</strong>g>of</str<strong>on</strong>g> the extract [12]. Following the initial lag period, as water is being removed<br />
from homogenates, the extracti<strong>on</strong> rate remains approximately c<strong>on</strong>stant, which suggest that this process is<br />
solubility-c<strong>on</strong>trolled. A comparis<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> operati<strong>on</strong>al solubilities (Table 2), defined as the slope <str<strong>on</strong>g>of</str<strong>on</strong>g> cumulative<br />
extracti<strong>on</strong> curves in Figure 1 and Figure 2 in the z<strong>on</strong>es where the extracti<strong>on</strong> rate is c<strong>on</strong>stant, shows that this is<br />
much higher when extracting dried powder than aqueous homogenate samples. This highlights the negative<br />
effect <str<strong>on</strong>g>of</str<strong>on</strong>g> water <strong>on</strong> the solubility <str<strong>on</strong>g>of</str<strong>on</strong>g> the lipidic (hydrophobic) comp<strong>on</strong>ents <str<strong>on</strong>g>of</str<strong>on</strong>g> H. pluvialis extract.<br />
Table 2. Operati<strong>on</strong>al solubility <str<strong>on</strong>g>of</str<strong>on</strong>g> astaxanthin in <strong>supercritical</strong> CO 2 (mg/kg) as a functi<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> extracti<strong>on</strong> c<strong>on</strong>diti<strong>on</strong>s.<br />
Temperature Pressure Operati<strong>on</strong>al solubility<br />
(ºC) (MPa) Dry powder Homogenate<br />
40 35 14 1,3<br />
40 45 19 1,6<br />
40 75 36 1,7<br />
70 35 17 1,6<br />
70 45 33 1,8<br />
70 75 65 1,5<br />
Astaxanthin c<strong>on</strong>centrati<strong>on</strong> in the extracts <str<strong>on</strong>g>of</str<strong>on</strong>g> aqueous homogenate samples depended also str<strong>on</strong>gly <strong>on</strong> extracti<strong>on</strong><br />
c<strong>on</strong>diti<strong>on</strong>s (Table 1). In this case, the purity <str<strong>on</strong>g>of</str<strong>on</strong>g> extracts decreased with extracti<strong>on</strong> temperature and was the<br />
highest at an intermediate pressure <str<strong>on</strong>g>of</str<strong>on</strong>g> 45 MPa. Furthermore, the extracti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> homogenates allowed higher