TY - JOUR
T1 - Response surface methodology to supercritical carbon dioxide extraction of astaxanthin from Haematococcus pluvialis
AU - Thana, Praiya
AU - Machmudah, Siti
AU - Goto, Motonobu
AU - Sasaki, Mitsuru
AU - Pavasant, Prasert
AU - Shotipruk, Artiwan
N1 - Funding Information:
This work was supported by Chulalongkorn University Graduate School and Thailand–Japan Technology Transfer Program (TJTTP).
PY - 2008/5
Y1 - 2008/5
N2 - Experimental design was used to investigate the effect of operating temperature (40-80 °C), operating pressure (30-50 MPa), and extraction time (1-4 h) of supercritical carbon dioxide (SC-CO2) extraction on astaxanthin yields and the extract antioxidant activity (IC50). The ranges of the factors investigated were 40-80 °C for the operating temperature (X1), 30-50 MPa for the operating pressure (X2), and 1-4 h for the extraction time (X3). The statistical analysis of the experiment indicated that pressure, extraction time, and the interaction between temperature and pressure (X1X2) had significant effect on astaxanthin yields. The central composite design showed that polynomial regression models were in good agreement with the experimental results with the coefficients of determination of 0.924 and 0.846 for astaxanthin yield and antioxidant activity, respectively. The optimal condition for astaxanthin yield within the experimental range of the variables studied was at 70 °C, 50 MPa, and 4 h. At this condition, the predicted amount of astaxanthin extracted was 23.04 mg/g (2.3 wt% or 83.78% recovery). For the effect of experimental extraction conditions on antioxidant activity, IC50 was used as an index, which is the concentration that gives a 50% reduction in the absorbance of the ABTS free radical. The analysis of the results showed that the interaction between the operating temperature and operating pressure (X1X2) was the only significant factor affecting the extract antioxidant activity. The statistical model gave the minimum point for antioxidant activity at 67 °C, 40.3 MPa, and 1.86 h of extraction, at which the value for 1/IC50 was 0.39 l/mg (or IC50 was 2.57 mg/l).
AB - Experimental design was used to investigate the effect of operating temperature (40-80 °C), operating pressure (30-50 MPa), and extraction time (1-4 h) of supercritical carbon dioxide (SC-CO2) extraction on astaxanthin yields and the extract antioxidant activity (IC50). The ranges of the factors investigated were 40-80 °C for the operating temperature (X1), 30-50 MPa for the operating pressure (X2), and 1-4 h for the extraction time (X3). The statistical analysis of the experiment indicated that pressure, extraction time, and the interaction between temperature and pressure (X1X2) had significant effect on astaxanthin yields. The central composite design showed that polynomial regression models were in good agreement with the experimental results with the coefficients of determination of 0.924 and 0.846 for astaxanthin yield and antioxidant activity, respectively. The optimal condition for astaxanthin yield within the experimental range of the variables studied was at 70 °C, 50 MPa, and 4 h. At this condition, the predicted amount of astaxanthin extracted was 23.04 mg/g (2.3 wt% or 83.78% recovery). For the effect of experimental extraction conditions on antioxidant activity, IC50 was used as an index, which is the concentration that gives a 50% reduction in the absorbance of the ABTS free radical. The analysis of the results showed that the interaction between the operating temperature and operating pressure (X1X2) was the only significant factor affecting the extract antioxidant activity. The statistical model gave the minimum point for antioxidant activity at 67 °C, 40.3 MPa, and 1.86 h of extraction, at which the value for 1/IC50 was 0.39 l/mg (or IC50 was 2.57 mg/l).
KW - Antioxidant activity
KW - Astaxanthin
KW - Central composite design
KW - Haematococcus pluvialis
UR - http://www.scopus.com/inward/record.url?scp=38949170980&partnerID=8YFLogxK
U2 - 10.1016/j.biortech.2007.05.062
DO - 10.1016/j.biortech.2007.05.062
M3 - Article
C2 - 17643298
AN - SCOPUS:38949170980
SN - 0960-8524
VL - 99
SP - 3110
EP - 3115
JO - Bioresource Technology
JF - Bioresource Technology
IS - 8
ER -