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Evaluation of microwave pre-treatment
in the extraction of Spirulina Platensis
oils by supercritical carbon dioxide.
17.09.2019
ICCPE'19
Lisbon, Portugal
Hugo Fabian Lobaton
Hugo Alexander Martinez
Spirulina Platensis
Cumaral, meta, Colombia
High value products
Phycocyanin
Exopolysaccharide
Fatty acid (10-200 mg g d.b)
Gamma linolenic acid (3-13 mg g d.b)
State of art
Cell disruption
Harvest
Extraction
State of art
• Extraction with super critical CO2 (ScCO2)
• No toxic
• Free solvent
• Temperature (31°c) and pressure (74 bars)
Materials and methods
Run Pre treatment Extraction conditions
1 Control Flow: 20g/min (18g CO2 + 2 g
ethanol-Polar lipids)
Extraction time: 3 hours
Temperature: 60°
Pressure: 360 bar
Spirulina weight 30 g
2 420 W, 5 min
3 420 W, 10 min
Kinetic model
𝑒1 = 𝑞 × 𝑦𝑠 0 ≤ 𝑞 ≤ 𝑞 𝑐 (1)
𝑒2 = 𝑥 𝑢 1 − 𝐶1 × 𝑒𝑥𝑝 −𝐶2 × 𝑞 𝑞 > 𝑞 𝑐 (2)
Sovová (Sovová, 2005)
Parameter
𝑒1 1st Phase, control by equilibrium
and external mass transfer
𝑞 Amount of solvent in certain time
𝑞 𝑐 Amount of solvent- end 1st
period
𝑦𝑠 Phase equilibrium constant
𝑒2 2 Phase, control by internal mass
transfer
𝑥 𝑢 Solute concentration
C1,C2 Model constants
Kinetic model
𝑟 = 1 − 𝐶1 × 𝑒𝑥𝑝
−𝐶2 × 𝑞 𝑐
2 (3)
𝑘 𝑠 𝑎 𝑠 = 1 − 𝑟 × 1 − 𝜀 × 𝑄 ×
𝐶2
𝑁 𝑚
(4)
𝐺 =
𝑒 𝑞 𝑐
𝑥 𝑢
(5)
Sovová (Sovová, 2005)
Parameter
r Pretreatment efficiency
𝒌 𝒔 𝒂 𝒔 Internal mass transfer
coefficient
𝑮 % open cells
𝑄 Volumetric flow
𝜀 Porosity
𝑁 𝑚 Solute mass fraction
𝑥 𝑢 Insoluble mass of solid
Results
Without pretreatment
Results
r(%) G(%) 𝒌 𝒔 𝒂 𝒔 Final yield (%) Error
Control 3 4 8.94e-5 13.46mg g-1 7.35%
420 W, 5 min 23.49 27.11 2.5 e-4 46.15 mg g-1 7.61%
420 W, 10 min 19.48 21.19 1.54e-4 33.9 mg g-1 8.34%
Results
420 W, 5 min 420 W, 10 min
Discussion
Spirulina
Pre treatment Extraction Yield Reference
1400 W-2 min
Chloroform/methanol
57 mg g-1 Pohndorf et al., 2016
Control 58.6 mg g-1
Chlorella
Pre treatment Extraction Yield Reference
800 W-1 min
ScCO2
47.3 mg g-1 (Dejoye et al., 2011)
Control 18.1 mg g-1
Discussion
Spirulina
Pre treatment Extraction Yield Reference
420 W-5 min 360 bar/60°c
ethanol 10%
46.15 mg g-1 This work
Grinding 300 bar/60°c
ethanol 100%
20 mg g-1 (Pereira et
al., 2004)
Future works
Fatty acids
Conclusions
• Microwave pretreatment helps to open the
cells
• 420 W-5 min prior to ScCO2 Yield 46.15 mg g-1
• Higher times degrade lipids
References
• Almquist, J., Cvijovic, M., Hatzimanikatis, V., Nielsen, J., & Jirstrand, M. (2014). Kinetic models in industrial biotechnology – Improving cell factory performance. Metabolic Engineering, 24,
38–60. doi://dx.doi.org/10.1016/j.ymben.2014.03.007
• Contreras-Flores, C., Peña-Castro, J. M., Flores-Cotera, L., & Cañizares-Villanueva, R. O. (2003). Advances in conceptual design of photobioreactors for microalgal culture. Avances En El
Diseño Conceptual de Fotobiorreactores Para El Cultivo de Microalgas, 28(8), 456+488.
• Dejoye, C., Vian, M. A., Lumia, G., Bouscarle, C., Charton, F., & Chemat, F. (2011). Combined extraction processes of lipid from Chlorella vulgaris microalgae: microwave prior to
supercritical carbon dioxide extraction. International Journal of Molecular Sciences, 12(12), 9332–9341. doi:10.3390/ijms12129332
• Esquivel-Hernández, D. A., Rodríguez-Rodríguez, J., Cuéllar-Bermúdez, S. P., García-Pérez, J. S., Mancera-Andrade, E. I., Núñez-Echevarría, J. E., … Parra-Saldívar, R. (2017). Effect of
Supercritical Carbon Dioxide Extraction Parameters on the Biological Activities and Metabolites Present in Extracts from Arthrospira platensis. Marine Drugs, 15(6), 174.
doi:10.3390/md15060174
• Golmakani, M.-T., Mendiola, J. A., Rezaei, K., & Ibáñez, E. (2012). Expanded ethanol with CO2 and pressurized ethyl lactate to obtain fractions enriched in γ-Linolenic Acid from
Arthrospira platensis (Spirulina). The Journal of Supercritical Fluids, 62, 109–115. doi:10.1016/J.SUPFLU.2011.11.026
• Lee, J.-Y., Yoo, C., Jun, S.-Y., Ahn, C.-Y., & Oh, H.-M. (2010). Comparison of several methods for effective lipid extraction from microalgae. Bioresource Technology, 101(1), S75–S77.
doi:10.1016/J.BIORTECH.2009.03.058
• McMillan, J. R., Watson, I. A., Ali, M., & Jaafar, W. (2013). Evaluation and comparison of algal cell disruption methods: Microwave, waterbath, blender, ultrasonic and laser treatment.
Applied Energy, 103, 128–134. doi:10.1016/J.APENERGY.2012.09.020
• Mendiola, J. A., Jaime, L., Santoyo, S., Reglero, G., Cifuentes, A., Ibañez, E., & Señoráns, F. J. (2007). Screening of functional compounds in supercritical fluid extracts from Spirulina
platensis. Food Chemistry, 102(4), 1357–1367. doi:10.1016/J.FOODCHEM.2006.06.068
• Patel, A., Gami, B., Patel, P., & Patel, B. (2017). Microalgae: Antiquity to era of integrated technology. Renewable and Sustainable Energy Reviews, 71, 535–547.
doi:10.1016/J.RSER.2016.12.081
• Pereira, A. P., Coelho, J. P., Mendes, R. L., Reis, A. D., Palavra, A. F., & Cardoso, M. T. (2004). Supercritical CO2 extraction of γ-linolenic acid (GLA) from the cyanobacterium Arthrospira
(Spirulina)maxima: experiments and modeling. Chemical Engineering Journal, 105(3), 147–151. doi:10.1016/j.cej.2004.10.006
• Pohndorf, R. S., Camara, Á. S., Larrosa, A. P. Q., Pinheiro, C. P., Strieder, M. M., & Pinto, L. A. A. (2016). Production of lipids from microalgae Spirulina sp.: Influence of drying, cell
disruption and extraction methods. Biomass and Bioenergy, 93, 25–32. doi:10.1016/J.BIOMBIOE.2016.06.020
• Rodrigues, M. S., Ferreira, L., Converti, A., Sato, S., & de Carvalho Carlos Monteiro, J. (2011). Influence of ammonium sulphate feeding time on fed-batch Arthrospira (Spirulina) platensis
cultivation and biomass composition with and without pH control. Bioresource Technology, 102(11), 6587–6592. doi://dx.doi.org/10.1016/j.biortech.2011.03.088
• Ronda, S. R., & Lele, S. S. (2008). Culture Conditions stimulating high γ-Linolenic Acid accumulation by Spirulina platensis. Brazilian Journal of Microbiology, 39(4), 693–697.
doi:10.1590/S1517-838220080004000018
• Roughan, P. G. (1989). Spirulina: A source of dietary gamma-linolenic acid? Journal of the Science of Food and Agriculture, 47(1), 85–93. doi:10.1002/jsfa.2740470110
• Sánchez-Camargo, A. P., Martinez-Correa, H., Paviani, L. C., & Cabral, F. A. (2011). Supercritical CO2 extraction of lipids and astaxanthin from Brazilian redspotted shrimp waste
(Farfantepenaeus paulensis). The Journal of Supercritical Fluids, 56(2), 164–173. doi://dx.doi.org/10.1016/j.supflu.2010.12.009
• Sovová, H. (2005). Mathematical model for supercritical fluid extraction of natural products and extraction curve evaluation. The Journal of Supercritical Fluids, 33(1), 35–52.
doi:10.1016/J.SUPFLU.2004.03.005
Thank you

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Iccep 2019

  • 1. Evaluation of microwave pre-treatment in the extraction of Spirulina Platensis oils by supercritical carbon dioxide. 17.09.2019 ICCPE'19 Lisbon, Portugal Hugo Fabian Lobaton Hugo Alexander Martinez
  • 3. High value products Phycocyanin Exopolysaccharide Fatty acid (10-200 mg g d.b) Gamma linolenic acid (3-13 mg g d.b)
  • 4. State of art Cell disruption Harvest Extraction
  • 5. State of art • Extraction with super critical CO2 (ScCO2) • No toxic • Free solvent • Temperature (31°c) and pressure (74 bars)
  • 6. Materials and methods Run Pre treatment Extraction conditions 1 Control Flow: 20g/min (18g CO2 + 2 g ethanol-Polar lipids) Extraction time: 3 hours Temperature: 60° Pressure: 360 bar Spirulina weight 30 g 2 420 W, 5 min 3 420 W, 10 min
  • 7. Kinetic model 𝑒1 = 𝑞 × 𝑦𝑠 0 ≤ 𝑞 ≤ 𝑞 𝑐 (1) 𝑒2 = 𝑥 𝑢 1 − 𝐶1 × 𝑒𝑥𝑝 −𝐶2 × 𝑞 𝑞 > 𝑞 𝑐 (2) Sovová (Sovová, 2005) Parameter 𝑒1 1st Phase, control by equilibrium and external mass transfer 𝑞 Amount of solvent in certain time 𝑞 𝑐 Amount of solvent- end 1st period 𝑦𝑠 Phase equilibrium constant 𝑒2 2 Phase, control by internal mass transfer 𝑥 𝑢 Solute concentration C1,C2 Model constants
  • 8. Kinetic model 𝑟 = 1 − 𝐶1 × 𝑒𝑥𝑝 −𝐶2 × 𝑞 𝑐 2 (3) 𝑘 𝑠 𝑎 𝑠 = 1 − 𝑟 × 1 − 𝜀 × 𝑄 × 𝐶2 𝑁 𝑚 (4) 𝐺 = 𝑒 𝑞 𝑐 𝑥 𝑢 (5) Sovová (Sovová, 2005) Parameter r Pretreatment efficiency 𝒌 𝒔 𝒂 𝒔 Internal mass transfer coefficient 𝑮 % open cells 𝑄 Volumetric flow 𝜀 Porosity 𝑁 𝑚 Solute mass fraction 𝑥 𝑢 Insoluble mass of solid
  • 10. Results r(%) G(%) 𝒌 𝒔 𝒂 𝒔 Final yield (%) Error Control 3 4 8.94e-5 13.46mg g-1 7.35% 420 W, 5 min 23.49 27.11 2.5 e-4 46.15 mg g-1 7.61% 420 W, 10 min 19.48 21.19 1.54e-4 33.9 mg g-1 8.34%
  • 11. Results 420 W, 5 min 420 W, 10 min
  • 12. Discussion Spirulina Pre treatment Extraction Yield Reference 1400 W-2 min Chloroform/methanol 57 mg g-1 Pohndorf et al., 2016 Control 58.6 mg g-1 Chlorella Pre treatment Extraction Yield Reference 800 W-1 min ScCO2 47.3 mg g-1 (Dejoye et al., 2011) Control 18.1 mg g-1
  • 13. Discussion Spirulina Pre treatment Extraction Yield Reference 420 W-5 min 360 bar/60°c ethanol 10% 46.15 mg g-1 This work Grinding 300 bar/60°c ethanol 100% 20 mg g-1 (Pereira et al., 2004)
  • 15. Conclusions • Microwave pretreatment helps to open the cells • 420 W-5 min prior to ScCO2 Yield 46.15 mg g-1 • Higher times degrade lipids
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