Extraction Yield Of Carotenoids Research Articles

Extraction and Emulsification of Carotenoids from Carrot Pomaces Using Oleic Acid.

This study aimed to use oleic acid-based ultrasonic-assisted extraction (UAE) to recover carotenoids from carrot pomace and emulsify the enriched-carotenoid oleic acid using spontaneous and ultrasonic-assisted emulsification. The extraction performance of oleic acid was compared with traditional organic solvents, including hexane, acetone, and ethyl acetate. The one-factor experiments were employed to examine the impact of UAE conditions, including liquid-to-solid ratios, temperature, ultrasonic power, and time, on the extraction yield of carotenoids and to find the conditional ranges for the optimization process. The response surface methodology was employed to optimize the UAE process. The second-order extraction kinetic model was used to find the mechanism of oleic acid-based UAE. After that, the enriched-carotenoid oleic acid obtained at the optimal conditions of UAE was used to fabricate nanoemulsions using spontaneous emulsification (SE), ultrasonic-assisted emulsification (UE), and SE-UE. The effect of SE and UE conditions on the turbidity of nanoemulsion was determined. Then, the physiochemical attributes of the nanoemulsion from SE, UE, and spontaneous ultrasonic-assisted emulsification (SE-UE) were determined using the dynamic light scattering method. The extraction yield of carotenoids from carrot pomace by using sonication was the highest. The adjusted optimal conditions were 39 mL/g of LSR, 50 °C, 12.5 min, and 350 W of ultrasonic power. Under optimal conditions, the carotenoid content attained was approximately 163.43 ± 1.83 μg/g, with the anticipated value (166 μg/g). The particle sizes of nanoemulsion fabricated at the proper conditions of SE, UE, and SE-UE were 31.2 ± 0.83, 33.8 ± 0.52, and 109.7 ± 8.24 nm, respectively. The results showed that SE and UE are suitable methods for fabricating nanoemulsions. The research provided a green approach for extracting and emulsifying carotenoids from carrot pomace.

Improving carotenoid extraction, stability, and antioxidant activity from Citrus sinensis peels using green solvents

Carotenoids have a wide range of applications in the food, pharmaceutical, and cosmetic industries as natural coloring agents and antioxidants. Consequently, industries are more concerned about extracting them from natural resources and by-products. The present research aimed to evaluate the extraction efficiency of carotenoids from orange peels using hydrophobic deep eutectic solvents (HDESs) as alternatives for organic solvents. The antioxidant capacity and color stability of HDESs extracts were monitored for 20 days and to intensify the extraction process, ultrasound-assisted extraction (UAE) was optimized using a response surface methodology (RSM). Menthol:Eucalyptol (Me:Eu) extract showed the highest carotenoid extraction yield [359.3 ± 3.5 mg/100 g of fresh weight (fw)], and also presented high stability during the storage period. HDESs extracts showed higher antioxidant capacity compared to hexane extracts, while Me:Eu extracts showed the lowest color variation (5.9 ± 0.2). Optimal parameters using Me:Eu were extraction time of 20 min, ultrasonic power of 120 W (60%), and solid–liquid ratio of 1:20 (g/mL) reaching a carotenoid content of 573.4 mg/100 gfw. While, C12:C8 optimal parameters were 10 min, 80 W (40%), and a solid–liquid ratio of 1:10 (g/mL), providing a carotenoid content of 183.7 mg/100 gfw. To establish if the solvents used are greener alternatives, the EcoScale was used and showed that UAE is a sustainable method to recover carotenoids using HDESs. Overall, the results showed that HDESs can improve carotenoid stability, and when combined with the intrinsic safety and edibility of their components, it makes these extracts appealing for food industry.

Vegetable oils as green solvents for carotenoid extraction from pumpkin (Cucurbita argyrosperma Huber) byproducts: Optimization of extraction parameters

Pumpkin pulp is the main waste generated by pumpkin seed growers. This agro-industrial waste is a valuable source of bioactive compounds, especially carotenoids (β-carotene, α-carotene, and lutein), which exhibit a broad spectrum of health-promoting effects. In this study, vegetable oils (canola, corn, and soybean oil) were used as green solvent alternatives to conventional organic solvents for carotenoid extraction from dried pumpkin pulp (DPP) waste. The highest carotenoid extraction yield (CEY) was obtained with canola oil, at a 1:10 DPP/oil ratio. Response surface methodology (RSM) was used to optimize the extraction process parameters (temperature, time, and stirring rate) through a Box-Behnken design (BBD) maximizing CEY in canola oil. The extraction temperature and stirring rate were found to have a significant linear and quadratic effect, respectively, on CEY. Optimum conditions were achieved at 21.8min, 250rpm, and 60°C. Under these optimized conditions, the estimated value for CEY was 378.1µg β-carotene equivalents/g of DPP, corresponding to 61.6% of the total carotenoid content present in the DPP. In contrast, the observed experimental value was 373.2µg β-carotene equivalents/g of DPP (61.2%). The experimental value was very close to the estimated value, which verifies the model's adequacy and fit. This study shows an alternative method to extract carotenoids from DPP with canola oil, obtaining an oil naturally enriched with carotenoids that could be used as a potential functional ingredient in the development of food, cosmetics, and medicinal products. PRACTICAL APPLICATION: Pumpkin by-products are a potential carotenoid source. Vegetable oil can be used as an alternative solvent for carotenoid extraction from pumpkin residues to obtain an enriched carotenoid oil that can be used to formulate food products.

Choline chloride-based deep eutectic solvents do not improve the ethanolic extraction of carotenoids from buriti fruit (Mauritia flexuosa L.)

The aim of the present study was to evaluate the effect of choline chloride-based deep eutectic solvents (DESs) as co-solvents for the ethanolic extraction of total carotenoids from buriti fruit (Mauritia flexuosa L.). Choline chloride-based DESs were synthesized by the heating method. The systems were prepared using ethanol and DESs as a co-solvent in concentrations of 0.5–70.0% (w/v). In addition, a control condition was performed using ethanol as the sole solvent. The total carotenoid concentration in the systems was determined by spectrophotometry at 450 nm. The results showed that the ethanol used without co-solvent obtained total carotenoid yields of 10.06 ± 0.03 mg/g for the buriti pulp and 10.43 ± 1.27 mg/g for the buriti peel. In turn, the use of choline chloride-based DESs as co-solvents did not increase the ethanolic extraction yield of carotenoids. However, it was observed that the buriti peel can be a rich source of carotenoids with yields comparable to the fruit. Thus, it is suggested that new green solvents be evaluated to increase the recovery of total carotenoids from buriti fruit using ecofriendly processes.

OPTIMIZATION OF CONDITIONS FOR CAROTENOIDS EXTRACTION FROM SHRIMP WASTE USING ORGANIC SOLVENT

In this study, factors affecting the extraction yield of carotenoids from dry shrimp waste by organic solvents such as ratio of hexane / acetone, ratio of solvent / shrimp waste, extraction temperature, extraction time, extraction method such as dynamic or static have been studied. The results showed that the solvent ratio hexane: acetone = 3: 1 gave the highest carotenoid yield. In this ratio of solvent’s mixture, the yield reached highest at temperature 60 °C for 2 hours, which was 44,64 µg / g raw shrimp waste (d.b.) (ratio of solvent to raw material 3/1). Ultrasound or vortexing gave higher extraction yield than in static conditions, which was 1.5- to 1.8- fold increase, respectively. At the ratio of solvent: dried shrimp = 4: 1, the amount of carotenoid recovered at 60°C for 2 hours reached 57.4 µg / g. However, if the shrimp waste was hydrolyzed with Alcalase at 50°C for 4 hours before extraction by solvent, the amount of carotenoid recovered achieved 149 µg / g of raw material

Application of pulsed electric fields to improve product yield and waste valorization in industrial tomato processing

The tomato processing industry strives to maximize product yield, keep energy costs and waste effluents to a minimum while maintaining high product quality. Pulsed Electric Field (PEF) processing increases plant cell permeability through electroporation and could be applied in tomato processing to facilitate peeling, increase juice yields and enhance valorization of tomato waste. PEF was applied to three different steps, of industrial tomato processing. In the first step, different PEF treatments (0.5–1.5 kV/cm, 0–8000 pulses, 15 μs pulse width) applied to whole tomatoes improved peeling, reducing the work required for peel detachment up to 72.3%. In the second step, PEF (0.5–2.5 kV/cm, 0–4000, pulses, 15 μs pulse width) applied to chopped tomatoes, increased tomato juice yield up to 20.5%. PEF was also applied to the residues of the first juicing step comprising seeds, peels and a fraction of tomato flesh, to further increase juice yield with the overall yield reaching 90.2%. In the third step the effects of PEF on the extraction of high added value compounds from juicing residues were studied. Carotenoid extraction yield increased up to 56.4%. Lycopene extraction increased from 9.84 mg lycopene/100 g to 14.31 mg/100 g tomato residue for a PEF treatment at 1.0 kV/cm for 7.5 ms. The concentration of extracted total phenolic compounds doubled (56.16 mg gallic acid/kg) with a 2 kV/cm, 700 pulses treatment. The increased antioxidant capacity was correlated to carotenoid concentration. Overall, targeted PEF pretreatments incorporated to industrial tomato processing lead to decreased energy demand and increased productivity.

Preparation of carotenoid extracts and nanoemulsions from Lycium barbarum L. and their effects on growth of HT-29 colon cancer cells

Lycium barbarum L., a traditional Chinese herb widely used in Asian countries, has been demonstrated to be protective against chronic diseases such as age-related macular degeneration. The objectives of this study were to determine the carotenoid content in L. barbarum by high-performance liquid chromatography–mass spectrometry, followed by preparation of a carotenoid nanoemulsion to evaluate the mechanism of inhibition on HT-29 colon cancer cells. The highest extraction yield of carotenoids was attained by employing a solvent system of hexane–ethanol–acetone (1:1:1, v/v/v). Nine carotenoids, including neoxanthin (4.47 μg g−1), all-trans-zeaxanthin and its cis-isomers (1666.3 μg g−1), all-trans-β-cryptoxanthin (51.69 μg g−1), all-trans-β-carotene and its cis-isomers (20.11 μg g−1), were separated within 45 min and quantified using a YMC C30 column and a gradient mobile phase of methanol–water (9:1, v/v) (A) and methylene chloride (B). A highly stable carotenoid nanoemulsion composed of CapryolTM 90, Transcutol®HP, Tween 80 and deionized water was prepared with a mean particle size of 15.1 nm. Characterization of zeaxanthin standard, blank nanoemulsion, carotenoid extract and carotenoid nanoemulsion by differential scanning calorimetry curves and Fourier transform infrared spectra revealed a good dispersion of zeaxanthin-dominated carotenoid extract with no significant chemical change after incorporation into nanoemulsion. The in vitro release kinetic study showed a higher release profile at pH 5.2 than at physiological pH 7.4, suggesting a rapid release of carotenoids in the acidic environment (pH 4.5–6.5) characteristic of tumors. Both the carotenoid nanoemulsion and the extract were effective at inhibiting growth of HT-29 colon cancer cells, with an IC50 of 4.5 and 4.9 μg ml−1, respectively. Also, both treatments could up-regulate p53 and p21 expression and down-regulate CDK2, CDK1, cyclin A and cyclin B expression and arrest the cell cycle at G2/M. The study may form a basis for further exploration of L. barbarum nanoemulsion in cancer treatment.

Optimisation of extraction conditions for recovering carotenoids and antioxidant capacity from Gac peel using response surface methodology

SummaryThe peel of Gac fruit is regarded as waste product in the processing of Gac although it contains high level of carotenoids and possesses a significant antioxidant capacity. This study optimised the extraction yields of carotenoids and antioxidant capacity from Gac peel. Different organic solvents were examined to determine the most suitable solvent for the extraction. The extraction conditions including time, temperature and solvent–solid ratio were then optimised for maximising extraction yields of carotenoids and antioxidant capacity from Gac peel using response surface methodology. Ethyl acetate was identified as the most suitable solvent. The optimal extraction time, temperature and solvent–solid ratio were 150 min, 40.7 °C and 80 mL g−1, respectively. The carotenoid extraction yield and the antioxidant capacity extraction yield were 271 mg/100 g DW and 737 μm TE/100 g DW, respectively. Thus, the extraction using ethyl acetate with the ratio of 80:1 (mL solvent per g Gac peel) for 150 min at 40.7 °C is suggested for recovering carotenoids and antioxidant capacity from Gac peel.

Experimental optimization of SC-CO2 extraction of carotenoids from Dunaliella salina

An experimental design procedure (based on the response surface method, RSM) was used to investigate the effect of pressure and temperature as operating parameters on the supercritical carbon dioxide (SC-CO2) extraction of carotenoids from Dunaliella salina microalgae. Using RSM method, 11 experiments were performed in random order and empirical correlation was developed. Results indicated that the effect of pressure on yield of extraction is much more than temperature. The most appropriate operating condition to obtain the best extraction yield of carotenoids was found at 400bar and 55°C (115.43μg/g dry microalgae). The recovery of carotenoids at optimum condition with supercritical extraction was half (47%) of the solvent extraction yield. The highest carotenoids/chlorophylls ratio (11.09) was obtained at 300bar and 30°C which show the selectivity of this technology. Under these operating conditions the separation and purification of the two extracted pigments facilitated and a higher selectivity is obtained.

Enhancement of pigment extraction from B. braunii pretreated using CO2 rapid depressurization.

Extraction of compounds from microalgae requires cell disruption as a pretreatment to increase extraction yield. Botryococcus braunii is a microalga with a significant content of carotenoids and other antioxidant compounds, such as chlorophylls. Cell disruption of B. braunii using CO2 rapid depressurization was studied as a pretreatment for the extraction of carotenoid and chlorophyll pigments. We studied the effect of temperature (21–49 °C) and pressure (6–13 MPa) during static compression on pigment recovery with supercritical CO2 at 40 °C, 30 MPa and solvent flow of 4.7 L NPT/min. Within the experimental region, the extraction yield of carotenoids and chlorophylls increased by 2.4- and 2.2-fold respectively. Static compression conditions of high pressure and low temperature increased the extraction of carotenoids and especially chlorophylls. We selected 21 °C and 13 MPa as the cell disruption condition, which produced 1.91 g/kg d.s. of carotenoids and 14.03 mg/kg d.s. of chlorophylls. Pretreated microalga gave a 10-fold higher chlorophyll extraction yield compared to the untreated sample. While for carotenoids and tocopherols were 1.25 and 1.14-fold higher, respectively. Additionally, antioxidant activity of pretreated microalga (33.22 mmol TE/kg oil) was significantly higher than the value for the untreated samples (29.11 mmol TE/kg oil) (p ≤ 0.05). Confocal microscopy images showed morphological differences between micro-colonies with and without disruption treatment, suggesting that partial cell disruption by rapid depressurization improved the extraction of microalga compounds.

Extraction of carotenoids from Lycium ferocissimum fruits for cotton dyeing: Optimization survey based on a central composite design method

Studies were carried out to assess the extraction yield of carotenoids from the African boxthorn (Lycium ferocissimum Miers, Solanaceae) fruits with different solvents and solvent mixtures, to optimize the extraction conditions for maximum recovery and to improve the extraction efficiency. Among other solvents, a mixture of hexane and acetone gave the highest carotenoid extraction. Extraction conditions, such as hexane percentage in hexane/acetone solvent mixture, solvent-solid ratio, and extraction time were optimized using a statistically designed experiment. A regression equation for predicting the carotenoid yield as a function of three extraction variables was derived by statistical analysis. The optimized conditions for maximum carotenoids yield were 45 % hexane in solvent mixture, solvent-solid ratio of 70 (ml/g) and extraction time 70 min. The dyeability of cotton with carotenoids extract has also been studied. Unmordant and postmordanted bleached cotton fabric with alum and ferrous sulphatewas dyed. Color measurements and fastness properties as light, rubbing and wash were tested.

Improving the extraction of carotenoids from tomato waste by application of ultrasound under pressure

The influence of the application of moderate pressure on the ultrasound assisted extraction of carotenoids from dry tomato pomace using a mixing of hexane/ethanol as solvent was investigated. Carotenoid extraction yield (CEY) increased by application of ultrasound and it was higher when static pressure was increased. In previous experiments it was establish that the optimum ultrasound amplitude, static pressure and sonication time for carotenoid extraction were 94μm of amplitude, 50kPa, 6min. These treatment conditions increased the extraction yield 143% in comparison with the control. Response surface methodology was used for optimization extraction temperature (25–45°C) and the proportion of hexane in the solvent (25%, 50%, 75%) for manosonication assisted extraction of carotenoids. The increment of CEY, the possibility of decreasing the percentage of hexane and the fact that the treatment did not cause degradation of carotenoid extracts are key benefits of manosonication assisted extraction of carotenoids from tomato.

Improving carotenoid extraction from tomato waste by pulsed electric fields.

In this investigation, the influence of the application of pulsed electric fields (PEFs) of different intensities (3–7 kV/cm and 0–300 μs) on the carotenoid extraction from tomato peel and pulp in a mixture of hexane:acetone:ethanol was studied with the aim of increasing extraction yield or reducing the percentage of the less green solvents in the extraction medium. According to the cellular disintegration index, the optimum treatment time for the permeabilization of tomato peel and pulp at different electric field strengths was 90 μs. The PEF permeabilization of tomato pulp did not significantly increase the carotenoid extraction. However, a PEF treatment at 5 kV/cm improved the carotenoid extraction from tomato peel by 39% as compared with the control in a mixture of hexane:ethanol:acetone (50:25:25). Further increments of electric field from 5 to 7 kV/cm did not increase significantly the extraction of carotenoids. The presence of acetone in the solvent mixture did not positively affect the carotenoid extraction when the tomato peels were PEF-treated. Response surface methodology was used to determine the potential of PEF for reducing the percentage of hexane in a hexane:ethanol mixture. The application of a PEF treatment allowed reducing the hexane percentage from 45 to 30% without affecting the carotenoid extraction yield. The antioxidant capacity of the extracts obtained from tomato peel was correlated with the carotenoid concentration and it was not affected by the PEF treatment.

Effects of electroplasmolysis treatment on chlorophyll and carotenoid extraction yield from spinach and tomato

In this study, the effects of electroplasmolysis on β-carotene, chlorophyll-a, chlorophyll-b and total chlorophyll contents of spinach extract and β-carotene and lycopene contents of tomatoes extracts were investigated. Three different voltage gradients (40, 60, 80V/cm) and three different application periods (4, 8, 12s) were used. The effects of water bath heating at different temperatures on the extraction yield of colorants were also studied. After pre-treatments, β-carotene, lycopene, chlorophyll-a, and chlorophyll-b extraction was performed. Total solid content, pH and titratable acidity of the spinach and tomato samples were also determined.In spinach, the highest extraction yield efficiency for β-carotene (19.7%) was obtained by water bath heating. The extraction yield efficiencies for chlorophyll-a, chlorophyll-b and total chlorophyll were 14.9%, 12.6% and 13.7% respectively, by the electroplasmolysis treatment at 60V/cm for 8s. In tomato, the highest increase in extraction yield efficiencies of β-carotene (139.1%) and lycopene (112.4%) was obtained by electroplasmolysis treatment at 80V/cm for 4s.

Process optimisation for recovery of carotenoids from tomato waste

Carotenoids constitute an important component of waste originating from tomato processing plants. Studies were carried out to assess the extraction yield of tomato waste carotenoids in different solvents and solvent mixtures and to optimise the extraction conditions for maximum recovery. A mixture of ethyl acetate and hexane gave the highest carotenoid extraction yield among the others examined. Extraction conditions, such as percentage of hexane in the solvent mixture of ethyl acetate and hexane, ratio of solvent to waste and particle size were optimised using a statistically designed experiment. A regression equation for predicting the carotenoid yield as a function of three extraction variables was derived by statistical analysis and a model with predictive ability of 0.97 was obtained. The optimised conditions for maximum carotenoid yield (37.5mgkg−1drywaste) were 45% hexane in solvent mixture, solvent mixture to waste ratio of 9.1:1 (v/w) and particle size 0.56mm.

Proximate composition and extraction of carotenoids and lipids from Brazilian redspotted shrimp waste ( Farfantepenaeus paulensis)

The chemical composition of redspotted shrimp ( Penaeus paulensis) waste was investigated. The shrimp waste (freeze-dried heads, shells and tails) was found to have high protein (49% d.w.) and ash (27% d.w.) contents, but a low lipid content (4.9% d.w.) although the latter was higher than those found in other kinds of shrimp captured in Brazil. The fatty acid compositions showed that the lipids had a high content of unsaturated fatty acids, mainly EPA (C20:5; n-3) and DHA (C22:6; n-3). In order to establish an efficient and environmentally friendly recovery process for the astaxanthin (principal carotenoid and antioxidant present in the waste), the following processes were examined: traditional solvent extraction (TSE), super-critical fluid extraction (SC-CO 2) and super-critical fluid extraction with co-solvent (SC-CO 2 + ethanol). The temperature and pressure conditions for all the SC-CO 2 extractions were 50 °C and 30.0 MPa. The results showed that the mixture of 60% (v/v) n-hexane:isopropyl alcohol gave the highest (53 mg/kg waste) carotenoid extraction yield as compared to acetone, SC-CO 2 and SC-CO 2 + ethanol. The SC-CO 2 showed the lowest extraction yield of astaxanthin, but the addition of the entrainer (10% w/w) produced an important effect, increasing the astaxanthin extraction to values of 57.9%, similar to extraction with acetone (63.3%).

Carotenoid production from Chlorococcum littorale in photoautotrophic cultures with downstream supercritical fluid processing

Carotenoid production from highly CO(2 )tolerant microalga Chlorococcum littorale in photoautotrophic cultures with downstream supercritical fluid processing was studied. Increasing temperature, increasing light intensity and decreasing CO(2) and O(2) gas concentrations enhanced growth rate under nitrate-rich conditions. Carotenoid content was insensitive to nitrate concentration, temperature and gas composition, but was greatly promoted by light intensity. Growth rate and carotenoid content had an optimum light intensity of ca. 120 micromol-photon * m(-2)s(-1). Separation of two sample cultures was studied by applying supercritical fluid extraction with CO(2 )and 10 mol% ethanol co-solvent. Extraction yield of carotenoids was 90% with 10 mol% ethanol at 333 K and 30 MPa. Selectivity of a sample with less lipid content (12.9 wt%) was five-fold higher than that with higher lipid content (29.4 w%).

Process optimization and extraction rate analysis of carotenoids extraction from rosehip fruit using supercritical CO 2

Carotenoids have been extracted from rosehip fruit using supercritical CO 2 at various extraction conditions. Carotenoids content in the extract was also determined by high-performance liquid chromatography (HPLC) method. Extraction was carried out at pressures of 150–450 bar, temperatures of 40–80 °C and CO 2 flow rates of 2–4 ml/min. A full 3 3 factorial design, in which pressure, temperature and CO 2 flow rate were used as design factors, coupled with statistical analysis of the results, by using analysis of variance (ANOVA), was used to optimize operating condition of carotenoids extraction in SC-CO 2. Extraction rate constant was calculated from the dependence of extraction yield on extraction time at 10, 20, 30, 50, 80, 110 and 150 min. Based on the experimental results, the total carotenoids extracted from rosehip fruit were found to be 10.35–20.88 mg/g fruit, and the maximum amount of carotenoids extracted was obtained at 80 °C, 450 bar and 4 ml/min. As determined by HPLC methods, the carotenoids extracted contained lycopene and β-carotene as main components, and small amount of lutein. The amount of lycopene, β-carotene and lutein extracted were 1.180–14.37 mg/g feed, 0.154–1.017 mg/g feed and 1.258–16.84 μg/g feed, respectively. The optimization results demonstrated that temperature was to be the influential variable on the extraction yield of carotenoids, with the statistical significant effect p-value was smaller than 0.05. For lycopene extracted, all variables (temperature, pressure and CO 2 flow rate) were to be the influential variables, but there is no possible interaction among variables. For β-carotene and lutein extracted, the influential variables were pressure and CO 2 flow rate without any interactions among variables. The mean extraction rate constant, k, of total carotenoids increased with increasing pressure and temperature, and the k values were (3.344–5.851) × 10 −3 min −1.

Carotenoids Extraction from Japanese Persimmon (Hachiya-kaki) Peels by Supercritical CO2 with Ethanol

The extraction of carotenoids from Japanese persimmon peels by supercritical fluid extraction (SFE), of which the solvent was CO(2), was performed. In order to enhance the yield and selectivity of the extraction, some portion of ethanol (5 - 20 mol%) was added as an entrainer. The extraction temperature ranged from 313 to 353 K and the pressure was 30 MPa. The effect of temperature on the extraction yield of carotenoids was investigated at 10 mol% of the ethanol concentration in the extraction solvent, and a suitable temperature was found to be 333 K among the temperatures studied with respect to the carotenoid yield. With increasing the entrainer amount from 0 to 10 mol% at a constant temperature (333 K), the carotenoid yield in the extraction was improved, whereas the selectivity of the extracted carotenoids was drastically depressed. We also conducted qualitative and quantitative analyses for the carotenoid components in the extract by HPLC, and analyzed the extraction behavior of each individual carotenoid (alpha-carotene, beta-carotene, beta-cryptoxanthin, lycopene, lutein, and zeaxanthin). The selectivity of each carotenoid changed with the elapsed time and its time evolution was dependent on the carotenoid component, indicating that the location profile and the content can be important factors to understand the SFE behavior of each carotenoid in persimmon peels.

Recovery of carotenoids from ensilaged shrimp waste

A method for fermentation of shrimp waste was standardized using a statistically designed experiment, with respect to three variables namely, levels of glucose and starter culture and time of fermentation. The optimized levels for achieving the desired pH was 20.5% glucose, 19.5 × 10 4 cells/g of starter culture and fermentation time of 70 h. Recovery of carotenoids from fermented and acid ensiled shrimp waste was assessed during 75 days of storage. Acid ensilaging resulted in the reduction of solvent extraction yield of carotenoids from 43.09 to 26.76 μg/g by the end of 75 days of storage. The yield of oil extracted carotenoids was higher in both types of silage at the end of 75 days storage compared to the initial yield, being 31.30 μg/g in fermented silage and 26.18 μg/g in acid silage. The results indicated the usefulness of fermentation as a method for stabilization and recovery of carotenoids in the shrimp waste.