Optimization of production of DHA from Crypthecodinium cohnii - - PowerPoint PPT Presentation

optimization of production of dha from crypthecodinium
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Optimization of production of DHA from Crypthecodinium cohnii - - PowerPoint PPT Presentation

Optimization of production of DHA from Crypthecodinium cohnii utilizing a dark fermentation effmuent Angelina Chalima, PhD Student, National T echnical University of Athens The accumulation of waste 19% Bioconversion of biowaste to high


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Angelina Chalima, PhD Student, National T echnical University of Athens

Optimization of production of DHA from Crypthecodinium cohnii utilizing a dark fermentation effmuent

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The accumulation of waste

19%

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Bioconversion of biowaste to high added-value products (carotenoids, omega-

3, biopolymers…)

Horizon 2020

Volatile Fatty Acids Platform from Biowaste by a dark fermentation process

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Dark fermentation

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Horizon 2020

Volatile Fatty Acids Platform from Biowaste by a dark fermentation process

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Crypthecodinium cohnii

  • Marine dinofmagellate
  • High lipid content (<70%)
  • High percentage of DHA

(docosahexaenoic acid)

  • Able to grow on glucose,

acetate, ethanol Used commercially for the production of DHA by Martek Bioscience

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So what did you actually do? We examined

  • C. cohnii

growth on the main VFA

  • f a DF

effmuent And then?

We developed a fermentation protocol in an actual DF effmuent

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Batch cultures of the strain

Acetic acid Propionic acid Butyric acid

Initial concentrations: 5- 50 g/L

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Low biomass production/ Specifjc tolerance to each VFA/ pH rise

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Fed-batch pH-auxostats

  • 15 g/L sodium

acetate

  • 7.5 g/L yeast

extract

  • 25 g/L sea salts

Acetic acid (33% v/v) Propionic acid (25% v/v) Butyric acid (25% v/v) DF ultrafjltrated effmuent Synthetic medium

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  • A. Chalima, et al. Integration of a dark fermentation

effmuent in a microalgal-based biorefjnery Applied Energy 241 (2019) 130-138

12 days 48 h

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Optimization

Culture conditions

Feed composition

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Optimization of lipid production (1. culture conditions)

  • Difgerent T

20-30oC

  • Difgerent nitrogen sources

Ammonium- Urea- Yeast extract- Nitrate

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Optimization of lipid production (1. culture conditions)

  • Difgerent C/N ratio

10-140

  • Chemical modulators

Ethanolamine Salicylic acid

C/N=50 DHA=36 %

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Optimization of lipid production (2. Feed)

  • Higher acid concentration

DF effmuent Total VFA (g/L) #1 13.8 #2 24.6

48 h 60 h

28%

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Conclusions

  • Acetate, butyrate, propionate
  • DF effmuent

(utilization of total organic content) Higher VFA concentration is favorable

  • Ammonium
  • 27 oC
  • C/N= 110
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Gazing into the future…

  • Use of DF effmuent as an initial medium for the

bioreactors  more effjcient utilization (in progress…)

  • Examination of utilization of lactic acid
  • Application of a two-stage fermentation protocol

“The future starts

today, not tomorrow…”

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Thank you very much!!

IndBioCat Group

Evangelos T

  • pakas

Maria Dimarogona Anthi karnaouri Natasa Zerva Alicia Paz Stratos Nikolaivits Georgia Asimakopoulou Grigoris Dedes Christina Pentari

Volatile W.P 6 group

Magdalini Krokida Thomas Dietrich

Tecnalia NTUA Biotechnology Lab