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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The objective ong>ofong> this work was to compare the scCO2 extraction ong>ofong> astaxanthin from an aqueous H. pluvialis homogenate with that from a dry powder counterpart. MATERIALS and METHODS Sample and sample analysis Disrupted dried cysts ong>ofong> H. pluvialis containing 4% water were supplied by Atacama BioNatural Products S.A. (Iquique, Chile). They were vacuum-packed and stored in a freezer at -15 ºC in the dark. The astaxanthin content in H. pluvialis’ powder was measured by extraction with acetone ong>ofong> 10 mg samples to exhaustion in several stages (up to the point where they were discolored). Prior to further analysis, the acetone contained in extract samples was removed in a nitrogen atmosphere. Supercritical CO2 extraction The extraction process was carried out in a one-pass, laboratory device (Thar Designs SFE-1L, Pittsburgh, PA) using food-grade (99.8% pure) CO2 (AGA S.A, Santiago, Chile). Dry powder H. pluvialis’ samples (1 g) mixed with 1.5 g ong>ofong> celite (Merck, Darmstadt, Germany) or aqueous homogenate samples (4 g suspensions containing 25% w/w ong>ofong> H. pluvialis’ powder) were loaded in a extraction vessel (50 cm 3 ) that was filled with glass spheres. Extractions were carried out using 10 g/min ong>ofong> CO2 at 40 or 70 °C and 35, 45, or 55 MPa. Cumulative yields ong>ofong> total extract and astaxanthin were determined as a function ong>ofong> process time by collecting, weighing, and analyzing extract samples in 1 h intervals up to a total extraction time ong>ofong> 10 h in the case ong>ofong> aqueous homogenate samples. Extract aliquots were collected in variable-time intervals during 4.5 h in scCO2 extractions ong>ofong> powder samples. Prior to further analyses, extracts were dried in a nitrogen atmosphere as done with acetone extract samples. Astaxanthin quantification Astaxanthin content in acetone or scCO2 extracts was determined in a UV/VIS spectrophotometer (Hach dr/2000, Loveland, CO) after dissolving them in acetone. The concentration ong>ofong> astaxanthin in the solutions was estimated using its optical extinction coefficient at λ = 470 nm in acetone (E 1% 1cm=2100) using eq. 1 [11]: x=Ay/ E 1% 1cm x 100 where x is the amount ong>ofong> pigment (g), A is the absorbance, and y the added amount ong>ofong> acetone (cm 3 ). RESULTS AND DISCUSSION Figure 1 shows cumulative extraction curves for astaxanthin as a function ong>ofong> specific CO2 consumption for the extraction ong>ofong> powder samples, and Table 1 summarizes values ong>ofong> astaxanthin recovery and concentration in extract samples for the 4.5-h extractions. Disrupted H. pluvialis’ cysts contained 32% w/w acetone extract, and 1.92% w/w astaxanthin. Results indicate a positive effect ong>ofong> system temperature and pressure on astaxanthin recovery that reached a maximum ong>ofong> ca. 61% at 70°C and 55 MPa. The positive effect ong>ofong> temperature can be explained by an increase in the vapor pressure ong>ofong> the solute with temperature, which facilitates its transfer to the scCO2 phase. On the other hand, the positive effect ong>ofong> pressure is due possibly to the increase in density and solvent power ong>ofong> CO2 that increases the solubility ong>ofong> oleoresin and astaxanthin in it. The effect ong>ofong> a 30 ºC increase in temperature outweighs the effect ong>ofong> a 20 MPa increase in pressure within our experimental region. The positive effects ong>ofong> temperature and pressure are consistent with those reported by others [7-10], although the magnitude ong>ofong> these effects varies from study to study. For example, Machmudah et al. [9] reported that an increase in temperature from 40 to 70 °C at 55 MPa imcreases astaxanthin recovery from ca. 15 to 78% (a 5-fold increase), a much larger effect that observed by us (an increase ong>ofong> only ca. 5%). On the other hand, an increase in pressure from 40 to 55 MPa at 70 °C increases astaxanthin recovery from ca. 25 to 78% (a 3-fold increase) [9], which is also much higher than the 7-17% increase observed in this work. The differences between studies

y (mg astaxantina/gr ong>microalgaong>) 12 10 8 6 4 2 550, 70 450,70 350, 70 550,40 450, 40 350,40 0 0 0,5 1 1,5 2 2,5 F (kg CO2/gr ong>microalgaong>) Figure 1. Cumulative extraction curves ong>ofong> dry Haematococcus pluvialis powder samples as a function ong>ofong> extraction temperature and pressure. Table 1. Recovery and concentration in extract ong>ofong> astaxanthin from Haematococcus pluvialis as a function ong>ofong> extraction conditions. Temperature Pressure Astaxanthin recovery (%) Astaxanthin concentration (%) (ºC) (MPa) Dry powder Homogenate Dry powder Homogenate 40 35 51.72 39.16 5.95 5.65 40 45 51.99 50.68 5.6 6.77 40 75 58.11 48.84 5.24 6.54 70 35 51.72 54.84 5.31 4.73 70 45 56.86 54.19 5.96 4.88 70 75 60.75 48.45 5.34 3.87 can be explained by differences between samples in cyst rupture degree, which affects extraction performance strongly [7]. Other important factor to consider is the selectivity ong>ofong> the extraction, characterized by the concentration ong>ofong> astaxanthin in extract samples (Table 1) or purity. In our experiments on dry H. pluvialis powder extraction, the purity ong>ofong> extracts samples changed little, being the highest (ca. 6%) at an intermediate condition (70°C and 45 MPa) that did not coincided with that for highest astaxanthin recovery. Unlike in this study, Machmudah et al. [9] reported a strong dependence ong>ofong> in extract purity on extraction conditions; as an example, it increases from ca. 3.5 to 12.5% (a 3.5-fold increase) when increasing temperature from 40 to 70°C at 55 MPa. Figure 2 shows cumulative extraction curves for astaxanthin as a function ong>ofong> specific CO2 consumption for the extraction ong>ofong> aqueous homogenate samples, and Table 1 summarizes values ong>ofong> astaxanthin recovery and concentration in extract samples for the 10-h extractions. In this case, the effect ong>ofong> extraction temperature and pressure on extraction rate and yield is not as evident or as easily explainable as in the extraction ong>ofong> powder samples (Fig. 1). Initial extraction rates ong>ofong> homogenates were smaller than those ong>ofong> dry powder samples, and extraction curves were S-shaped. The lag-period when extracting homogenates may be associated to a negative

The objective <str<strong>on</strong>g>of</str<strong>on</strong>g> this work was to compare the sc<strong>CO2</strong> extracti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> astaxanthin from an aqueous H. pluvialis<br />

homogenate with that from a dry powder counterpart.<br />

MATERIALS and METHODS<br />

Sample and sample analysis<br />

Disrupted dried cysts <str<strong>on</strong>g>of</str<strong>on</strong>g> H. pluvialis c<strong>on</strong>taining 4% water were supplied by Atacama BioNatural Products S.A.<br />

(Iquique, Chile). They were vacuum-packed and stored in a freezer at -15 ºC in the dark. The astaxanthin c<strong>on</strong>tent<br />

in H. pluvialis’ powder was measured by extracti<strong>on</strong> with acet<strong>on</strong>e <str<strong>on</strong>g>of</str<strong>on</strong>g> 10 mg samples to exhausti<strong>on</strong> in several<br />

stages (up to the point where they were discolored). Prior to further analysis, the acet<strong>on</strong>e c<strong>on</strong>tained in extract<br />

samples was removed in a nitrogen atmosphere.<br />

Supercritical <strong>CO2</strong> extracti<strong>on</strong><br />

The extracti<strong>on</strong> process was carried out in a <strong>on</strong>e-pass, laboratory device (Thar Designs SFE-1L, Pittsburgh, PA)<br />

using food-grade (99.8% pure) <strong>CO2</strong> (AGA S.A, Santiago, Chile). Dry powder H. pluvialis’ samples (1 g) mixed<br />

with 1.5 g <str<strong>on</strong>g>of</str<strong>on</strong>g> celite (Merck, Darmstadt, Germany) or aqueous homogenate samples (4 g suspensi<strong>on</strong>s c<strong>on</strong>taining<br />

25% w/w <str<strong>on</strong>g>of</str<strong>on</strong>g> H. pluvialis’ powder) were loaded in a extracti<strong>on</strong> vessel (50 cm 3 ) that was filled with glass spheres.<br />

Extracti<strong>on</strong>s were carried out using 10 g/min <str<strong>on</strong>g>of</str<strong>on</strong>g> <strong>CO2</strong> at 40 or 70 °C and 35, 45, or 55 MPa. Cumulative yields <str<strong>on</strong>g>of</str<strong>on</strong>g><br />

total extract and astaxanthin were determined as a functi<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> process time by collecting, weighing, and<br />

analyzing extract samples in 1 h intervals up to a total extracti<strong>on</strong> time <str<strong>on</strong>g>of</str<strong>on</strong>g> 10 h in the case <str<strong>on</strong>g>of</str<strong>on</strong>g> aqueous homogenate<br />

samples. Extract aliquots were collected in variable-time intervals during 4.5 h in sc<strong>CO2</strong> extracti<strong>on</strong>s <str<strong>on</strong>g>of</str<strong>on</strong>g> powder<br />

samples. Prior to further analyses, extracts were dried in a nitrogen atmosphere as d<strong>on</strong>e with acet<strong>on</strong>e extract<br />

samples.<br />

Astaxanthin quantificati<strong>on</strong><br />

Astaxanthin c<strong>on</strong>tent in acet<strong>on</strong>e or sc<strong>CO2</strong> extracts was determined in a UV/VIS spectrophotometer (Hach<br />

dr/2000, Loveland, CO) after dissolving them in acet<strong>on</strong>e. The c<strong>on</strong>centrati<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> astaxanthin in the soluti<strong>on</strong>s was<br />

estimated using its optical extincti<strong>on</strong> coefficient at λ = 470 nm in acet<strong>on</strong>e (E 1% 1cm=2100) using eq. 1 [11]:<br />

x=Ay/ E 1% 1cm x 100<br />

where x is the amount <str<strong>on</strong>g>of</str<strong>on</strong>g> pigment (g), A is the absorbance, and y the added amount <str<strong>on</strong>g>of</str<strong>on</strong>g> acet<strong>on</strong>e (cm 3 ).<br />

RESULTS AND DISCUSSION<br />

Figure 1 shows cumulative extracti<strong>on</strong> curves for astaxanthin as a functi<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> specific <strong>CO2</strong> c<strong>on</strong>sumpti<strong>on</strong> for the<br />

extracti<strong>on</strong> <str<strong>on</strong>g>of</str<strong>on</strong>g> powder samples, and Table 1 summarizes values <str<strong>on</strong>g>of</str<strong>on</strong>g> astaxanthin recovery and c<strong>on</strong>centrati<strong>on</strong> in<br />

extract samples for the 4.5-h extracti<strong>on</strong>s. Disrupted H. pluvialis’ cysts c<strong>on</strong>tained 32% w/w acet<strong>on</strong>e extract, and<br />

1.92% w/w astaxanthin. Results indicate a positive effect <str<strong>on</strong>g>of</str<strong>on</strong>g> system temperature and pressure <strong>on</strong> astaxanthin<br />

recovery that reached a maximum <str<strong>on</strong>g>of</str<strong>on</strong>g> ca. 61% at 70°C and 55 MPa. The positive effect <str<strong>on</strong>g>of</str<strong>on</strong>g> temperature can be<br />

explained by an increase in the vapor pressure <str<strong>on</strong>g>of</str<strong>on</strong>g> the solute with temperature, which facilitates its transfer to the<br />

sc<strong>CO2</strong> phase. On the other hand, the positive effect <str<strong>on</strong>g>of</str<strong>on</strong>g> pressure is due possibly to the increase in density and<br />

solvent power <str<strong>on</strong>g>of</str<strong>on</strong>g> <strong>CO2</strong> that increases the solubility <str<strong>on</strong>g>of</str<strong>on</strong>g> oleoresin and astaxanthin in it. The effect <str<strong>on</strong>g>of</str<strong>on</strong>g> a 30 ºC<br />

increase in temperature outweighs the effect <str<strong>on</strong>g>of</str<strong>on</strong>g> a 20 MPa increase in pressure within our experimental regi<strong>on</strong>.<br />

The positive effects <str<strong>on</strong>g>of</str<strong>on</strong>g> temperature and pressure are c<strong>on</strong>sistent with those reported by others [7-10], although the<br />

magnitude <str<strong>on</strong>g>of</str<strong>on</strong>g> these effects varies from study to study. For example, Machmudah et al. [9] reported that an<br />

increase in temperature from 40 to 70 °C at 55 MPa imcreases astaxanthin recovery from ca. 15 to 78% (a 5-fold<br />

increase), a much larger effect that observed by us (an increase <str<strong>on</strong>g>of</str<strong>on</strong>g> <strong>on</strong>ly ca. 5%). On the other hand, an increase<br />

in pressure from 40 to 55 MPa at 70 °C increases astaxanthin recovery from ca. 25 to 78% (a 3-fold increase)<br />

[9], which is also much higher than the 7-17% increase observed in this work. The differences between studies

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