Production of Fucoxanthin from Microalgae Isochrysis galbana of Djibouti: Optimization, Correlation with Antioxidant Potential, and Bioinformatics Approaches
Abstract
:1. Introduction
2. Results
2.1. Optimization of Growth Parameters
2.2. Correlation between Antioxidant Activity and Compound Content
2.3. Optimization of Experimental Conditions by Experimental Design
2.4. In Silico Study
3. Discussion
4. Material and Methods
4.1. Cultivation of the Microalgae I. galbana
4.2. Procedure for Obtaining Extracts for Analyses
4.3. Determination of Antioxidant Activity by the DPPH Method
4.4. Estimation of Carotenoid Content
4.5. Total Phenolic Content
4.6. Quantification of Fucoxanthin
4.7. Statistical Studies
- Factor 1 = T: temperature (25 °C and 30 °C);
- Factor 2 = pH: pH (6.5 and 7.5);
- Factor 3 = light intensity: LI (100 µmol/m2/s and 500 µmol/m2/s);
- Factor 4 = air flow rate: AFR (0.5 L/min and 1.0 L/min);
- Factor 5 = CO2 flow rate: CO2FR (0.1–0.2 L/min).
- A mean: a0;
- 5 main effects for each factor: ai;
- 10 interactions of order 2: aij;
- 10 interactions of order 3: aijk;
- 5 interactions of order 4: aijkl;
- 1 interaction of order 5: aijklm.
4.8. In Silico Study
5. Conclusions
Supplementary Materials
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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Culture Medium | Dry Weight Biomass (g/L) | DPPH IC50 (μg/mL) | Carotenoids Content (mg/g) | Total Phenolic Content (mg/100 g) | Fucoxanthin (mg/g) |
---|---|---|---|---|---|
Natural Seawater (Djibouti) | 0.65 ± 0.12 a | 481 ± 25 a | 9.9 ± 0.2 a | 12.0 ± 1.1 a | 2.8 ± 0.5 a |
3N-BBM+V Medium | 0.88 ± 0.17 a,b,c | 438 ± 20 a,b | 11.5 ± 1.3 b | 20.0 ± 1.8 b | 4.6 ± 0.8 b |
ASP-M Medium | 0.82 ± 0.16 a,b,c | 435 ± 25 a,b | 11.7 ± 1.2 b | 19.2 ± 1.7 b | 4.8 ± 0.7 b |
CHU-10 Medium | 0.91 ± 0.18 b,c | 440 ± 25 a,b | 11.5 ± 1.1 b | 20.1 ± 1.8 b | 5.0 ± 0.8 b |
Conway Medium | 0.92 ± 0.18 b,c | 415 ± 25 b,c | 13.1 ± 1.5 b,c | 20.3 ± 2.0 b | 5.0 ± 0.6 b |
Erdschreiber Medium | 0.95 ± 0.19 b,c | 405 ± 20 c | 12.8 ± 1.8 b,c | 20.1 ± 2.1 b | 5.2 ± 0.5 b |
Guillard F/2 Medium | 1.22 ± 0.21 c,d | 304 ± 15 d | 16.6 ± 2.4 d | 20.5 ± 1.8 b | 7.8 ± 1.0 c |
PM Medium | 0.82 ± 0.16 a,b,c | 421 ± 30 b,c | 11.2 ± 1.2 a,b | 19.1 ± 1.8 b | 4.6 ± 0.5 b |
Walne Medium | 1.28 ± 0.22 c,d | 285 ± 15 e | 15.4 ± 1.8 d | 23.6 ± 2.5 b,c | 7.8 ± 0.8 c |
Water Culture Medium | 1.15 ± 0.20 c,d | 413 ± 25 b,c | 14.2 ± 1.6 c,d | 19.4 ± 1.8 b | 5.5 ± 0.5 b |
Matrix | Z2 | Z3 | Z4 | Z1 |
---|---|---|---|---|
Z2 | 1 | |||
Z3 | 0.660 | 1 | ||
Z4 | 0.943 | 0.794 | 1 | |
Z1 | −0.913 | −0.706 | −0.970 | 1 |
Proteins | 3FS1 | 3L2C | 8BBK |
---|---|---|---|
Binding affinity (kcal/mol) | −7.3 | −9.4 | −9.3 |
pKi | 5.35 | 6.89 | 6.82 |
Ligand efficiency (kcal/mol) | 0.1521 | 0.1958 | 0.1938 |
Ligand–protein interactions | 25 | 10 | 31 |
Number of π-σ bond | 0 | 0 | 1 |
Number of alkyl bond | 15 | 0 | 10 |
Number of π-alkyl bond | 4 | 8 | 4 |
Number of conventional hydrogen bond | 1 | 1 | 1 |
Number of carbon–hydrogen bond | 0 | 1 | 0 |
Number of van der Waals bond | 5 | 0 | 15 |
Work | Reference | Year | Study Objective | Methodology | Key Results | Quantity of Fucoxanthin | Implications |
---|---|---|---|---|---|---|---|
1 | Médine et al. [45] | 2019 | Examine the extraction of fucoxanthin from I. galbana for obesity prevention. | Comparison of solvents (methanol, ethanol, petroleum ether, n-hexane). Optimization of extraction time. | Best yields with methanol (6.282 mg/g DW) and ethanol (4.187 mg/g DW). Optimal extraction in 10 min with 100% ethanol. | 6.282 mg/g DW (methanol), 4.187 mg/g DW (ethanol) | I. galbana is a promising source of fucoxanthin for the food industry. |
2 | Pereira et al. [46] | 2021 | Optimize industrial-scale fucoxanthin production. | Cultivation in 15 m3 tubular photobioreactors. Seasonal comparison between P. tricornutum and T. lutea. | P. tricornutum achieved 2.87 g DW L−1 and 0.7% DW fucoxanthin (7 mg/g DW) in fall/winter. T. lutea was more productive in spring/summer. | 7 mg/g DW | Feasibility of continuous fucoxanthin production year-round. |
3 | Gao et al. [47] | 2020 | Optimize fucoxanthin production in T. lutea. | Batch and continuous experiments, adjusting parameters like temperature, irradiation, and dilution rate. | Maximum productivity at 30 °C and 300 μmol m−2 s−1. High dilution rates (0.53 and 0.80 d−1) and light absorption of 2.23 mol m−2 d−1 favored high fucoxanthin content. | 16.39 mg/g DW | Light absorption can predict fucoxanthin content. |
4 | Mohamadnia et al. [48] | 2021 | Optimize fucoxanthin production in T. lutea using response surface methodology. | Adjustment of culture conditions in 1 L batch photobioreactors with polynomial second-order modeling. | Optimal conditions: salinity 36.27 g L−1, starch 3.90 g L−1, nitrate 0.162 g L−1. | 79.4 mg/g DW | Optimization of culture parameters to maximize fucoxanthin production. |
5 | Mohamadnia et al. [49] | 2022 | Refine fucoxanthin production using response surface methodology (RSM). | Adjustment of concentrations of glutamic acid, trisodium citrate, succinic acid, sodium aspartate, and pyruvate. | Optimal concentrations: sodium aspartate 7.5 mM, sodium pyruvate 7.5 mM, glutamic acid 3.29 mM. Productivity of 22.4 mg L−1 day−1. | 22.4 mg L−1 day−1 | Metabolic optimization strategies to increase fucoxanthin production. |
6 | McElroy et al. [50] | 2023 | Integrate biorefining to valorize Saccharina latissima biomass. | Optimized extraction of fucoxanthin at 40 MPa. Integration with mannitol and alginate extraction. Life cycle analysis. | 4.15% yield for fucoxanthin. Extraction of 67.27% to 69.38% of alginates. Reduction in environmental impact identified. | 41.5 mg/g DW | Integrated biorefining processes to reduce environmental footprint. |
7 | Xia et al. [51] | 2023 | Assess the impact of CO2 concentration and frequency on fucoxanthin production. | Comparison of continuous and intermittent CO2 supply at different concentrations. | Continuous CO2 at 5% achieved maximum biomass productivity (0.33 g L−1 day−1). Intermittent CO2 at 5% optimized fucoxanthin accumulation. | 0.56 mg/g DW | Improved fucoxanthin accumulation with intermittent CO2 supply. |
8 | Bo et al. [52] | 2023 | Study the effect of spermidine on fucoxanthin biosynthesis in Isochrysis sp. | Addition of spermidine under different light intensities and assessment of cell proliferation and pigment synthesis. | Optimal cell density of 5.40 × 106 cells/mL after 11 days. Maximum diadinoxanthin (1.09 mg/g DW) and fucoxanthin under low light intensity. | 6.11 mg/g DW | Spermidine enhances fucoxanthin production and mitigates photosystem damage under high light intensity. |
9 | Garcia-García et al. [53] | 2024 | Explore extraction of fucoxanthin and DHA from T. lutea using green solvents. | Use of green solvents and advanced extraction techniques, such as ultrasonic-assisted extraction with 2-methyltetrahydrofuran and ethanol. | High extraction yields of fucoxanthin and DHA. 2-Methyl-tetrahydrofuran-enriched extracts showed better composition. | High (exact quantity not provided) | Advanced extraction techniques to preserve bioactivity of extracts. |
10 | Manochkumar et al. [54] | 2024 | Optimize fucoxanthin production using machine learning. | Development of a machine learning model to predict fucoxanthin yield based on phytohormone supplementation. | Random Forest and ANN models showed improved accuracy with hormone descriptors. | - | Combining UV spectrometry and ML algorithms for precise fucoxanthin predictions and production optimization. |
11 | This work | - | Optimize fucoxanthin production from I. galbana and validate antioxidant potential. | Test various culture media. Evaluate antioxidant potential. Use PCA and regression models. Optimize growth conditions (air flow rate and CO2 flow). Perform molecular docking analysis. | Walne and Guillard media most effective. Strong correlation between antioxidant activity and fucoxanthin. Air flow rate and CO2 flow are key factors. Fucoxanthin interacts with antioxidant proteins. | 13.4 mg/g DW | Improved production methods. Validated antioxidant benefits. Insights for future research and applications. |
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Mohamed Abdoul-Latif, F.; Ainane, A.; Achenani, L.; Merito Ali, A.; Mohamed, H.; Ali, A.; Jutur, P.P.; Ainane, T. Production of Fucoxanthin from Microalgae Isochrysis galbana of Djibouti: Optimization, Correlation with Antioxidant Potential, and Bioinformatics Approaches. Mar. Drugs 2024, 22, 358. https://doi.org/10.3390/md22080358
Mohamed Abdoul-Latif F, Ainane A, Achenani L, Merito Ali A, Mohamed H, Ali A, Jutur PP, Ainane T. Production of Fucoxanthin from Microalgae Isochrysis galbana of Djibouti: Optimization, Correlation with Antioxidant Potential, and Bioinformatics Approaches. Marine Drugs. 2024; 22(8):358. https://doi.org/10.3390/md22080358
Chicago/Turabian StyleMohamed Abdoul-Latif, Fatouma, Ayoub Ainane, Laila Achenani, Ali Merito Ali, Houda Mohamed, Ahmad Ali, Pannaga Pavan Jutur, and Tarik Ainane. 2024. "Production of Fucoxanthin from Microalgae Isochrysis galbana of Djibouti: Optimization, Correlation with Antioxidant Potential, and Bioinformatics Approaches" Marine Drugs 22, no. 8: 358. https://doi.org/10.3390/md22080358