Microalgae for an industrial desert ecology

Microalgae for 'Carbon negative' 
- bioelectricity
- energy storage
- potable water
- biodiesel

- biohydrogen
- biochar eg.water filtration, Atmospheric Water Harvesting (AWH)->dew irrigation system
- 'Greener steel'
Plus CDR credits (additional revenue stream)

  • options for pigments and bioactive compounds using additional microalgae strains
  • protein usually uses the whole plant eg. Spirulina

 

Biochemistry
Photosynthesis of microalgae->carbohydrates->pretreatment with enzymes eg.cellulase->cell wall breakdown->bioavailable carbohydrates(glucose) for bacteria + biochar catalyst->dark fermentation (DF) of carbohydrates (via at least 2 metabolic pathways)->Hydrogen evolution (production) with Hydrogenase, combining protons and electrons to form molecular hydrogen (but the reaction is also reversible: H2<->2H+ + 2e-)

NOTES

- Modular and scalable system, mostly solid state (more research needed on the hardware)
- No electricity/unpowered process (for both desalination and H2, other than the seawater pumps) compared to powered desal and electrolysis but maybe more complex workflow, expensive hardware and lower yields! Also, powered electrolysis can be done using seawater, but most tech of the day use potable water
- pretreatment (before the initial lipid extraction) can be physical, chemical or biological but I prefer biological for it's 'Green chemistry' and energy efficiency

- some naturally occurring microalgae strains perform better than GE strains in brine (halotolerant/halophilic)

- The hunt is finding the best strain that grows in brine, fast growth rate, high in lipids and carbohydrates, preferably endemic and high surface area after Pyrolysis, eg. Nanochloropsis oceanica

  • ticks most (?all) the boxes
  •  genome sequenced

- There is also a possibility of using a different strain of Nanochloropsis, unknown, studied in an academic paper on supercaps (see below), which achieved at Highest Temperature Treatment (HTT) 900degsC during pyrolysis, with KOH activation afterwards, 3187m2/g surface area which is off the charts! This could be a contender for Atmospheric Water Harvesting (AWH) panels but would probably need to be directly pyrolysed with no biorefinery cascade     

- surface area will also depend on pretreatment used for biodiesel, protein, biohydrogen and biogas production, and the pyrolysis tech eg. Charcell (https://metamorf.engineering/) (with heat exchanger for bioelectricity), and pyrolysis temperature. Activation also plays in - KOH V steam activation

- A suitable halotolerant bacteria is needed for DF
- The quality of the Biochar is uncertain since cell walls are broken down during pretreatment of microalgae which will decrease surface area, important for catalyst efficiency (and other applications eg.water filtration, too)
- The biorefinery uses a cascade of microalgae processing: lipid extraction->Biodiesel->Protein->Biohydrogen + Biogas (using DF)-> waste biomass->dried-> pelletised (doped with ?Fe3O4for DF catalyst)->Pyrolysis-> biochar pellets->various applications, with possible steam activation for air and water filtration

  • For the DF catalyst: (doped) biochar pellets->steam activated->milled (for huge surface area/microbial habitat)->added to DF process
  • For the H2 storage media (biochar Mn MOF):biochar pellets->steam activated->organic linkers and Mn salts added in 'One pot'->Carbon-Oxygen-Metal (C-O-M) bonding->washed->dried->H2 storage tank pellet media for increased volumes of H2 storage, ?more stable at ambient temperature

Both of the above processes need more research!!
- supply and demand of all the products needs to be balanced which will vary from one place/economy to the next
    - buffers exist to balance energy
        - energy storage (RFD)
        - H2 storage
        - bioelectricity production (microalgae waste biomass fuel pellets input) 

 

FYI

Try doing an academic 'Research' search in perplexity.ai for:

"Nanochloropsis oceanica: Integrated Biorefinery cascade for Biodiesel, Protein, Biohydrogen, Biogas and Biochar Production in Brine Systems"

Surface area off the charts (p.5). Supercaps, anyone?
Indicates that potentially the Nanochloropsis genus may have a relatively high surface area after the biorefinery cascade compared to other microalgae genus's if pyrolysed at 900 degsC. Self-doping is a new concept to me that warrants further research. Doping can also be additional before or after pyrolysis but from what I have read usually before. Biochar-based MOFs are built after pyrolysis which needs both organic linkers and metal salts to achieve C-O-M bonds. KOH (a strong base) activation, or acids, such as HCl, can be used for post-pyrolysis activation but could be substituted with steam activation which is cheaper, cleaner but usually produces relatively lower surface areas.
3187 m² per g after activation.pdf
Adobe Acrobat Document 14.4 MB
Novel supplementation of Fe3 O4 -doped green carbonized nanoparticles on hydrogenases genes and microbial biodiversity for enhancing biohydrogen yield in dark fermentation
Novel supplementation of Fe3 O4 -doped g
Adobe Acrobat Document 1.7 MB

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