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Doc Williamon said:B. braunii are notoriously slow growing despite the high percentage of lipid contents. Did "four or five harvest cycles" represent the entire harvest number in the six months work with the species? I was very pleased to hear that it was "like pea soup", since the DoE and DoA are currently running a competition to see if someone can concentrate a one gram per liter solution of algae into a 20% solids suspension, at something less than current industry capital and operating costs, therefore I would like to know, were you speaking of a post-concentration process thickness, or the raw batch after a month or more of cultivation?
Hello Doc . Thanks for chiming in. "pea soup" might have been an unfortunate reference, I was referring to the optical density, not the mass density. The raw harvested solution had about a 1% mass density.
I chose B braunii because I assumed the high lipid content would be helpful given my limited means of processing. :) But I never got anywhere near the theoretical limit for Bb [about 60-70%. IIRC]. I think the highest I saw was about 20% by weight. That was some years ago now so I can only offer my best recollections.
For that matter, with the high lipid content were the B. braunii predominantly floating on the surface of the growth medium, or were you using a churning dispersion method of solve the self-shadowing problem that prevented the natural floating buoyancy?
I was using unlimited aeration to provide churning dispersion. While not applicable at scale [too much energy demand per harvest cycle], at the time I was focused on the bioreactor design and didn't worry about the energy. But that was one nagging issue that I never resolved satisfactorily. I was always worried about the energy demand required for circulation, in practice. I decided that a very low-power mechanical solution [stirring] was the only viable option. I intended to minimize the air flow and consequential energy demand by using a CO2-enriched air supply.
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