초록
<P><B>Abstract</B></P> <P>Robust microalgae cultivation at industrial scale needs complex scale-up of photobioreactors since the same yields obtained at lab-scale are hardly reached during pilot or industrial production. In this paper we propose a procedure based on Buckingham π-theorem to perform the scale-up of photobioreactors used to cultivate <I>Chlorella Vulgaris</I> fed by CO<SUB>2</SUB> and wastewater rich in glycerol. This theoretical approach is usually overlooked in favor of the synergy of modeling tailored on the process and piloting, but it grants excellent generalizability. An experimental campaign at three levels was designed and carried out to evaluate the characteristic dimensionless numbers individuated by the theoretical formulation. Since scale-up regards both geometrical dimensions and type of reactor, passing from lab-scale stirred tanks (STRs) to pilot scale tubular and airlift, particular attention was devoted to defining characteristic lengths inside the dimensionless numbers. Moreover, since scale-up also regards the operating mode, scaling from discontinuous to semi-continuous to continuous, some interesting dimensionless numbers arise other than R e , S h , <SUB> D a I I </SUB> . They are mainly related to the type of biological process and its operating mode and are the ratios O<SUB>2</SUB>/CO<SUB>2</SUB> and T/T<SUB>opt</SUB>, the ratio between the incident light intensity and the saturation constant, the absorbance, the ratio between the final and the initial concentration c/c<SUB>0</SUB>, the ratio between the maximum increase in cell population and its initial concentration, the ratio between the estimated specific kinetic constant and a variable representing the characteristic time of mixing inside the chosen reactor.</P> <P>Preliminary outdoor tests confirmed the operability of the scaled-up airlift reactors reaching c/c<SUB>0</SUB> = 5.3–7.5, with c = 1.15 g L<SUP>−1</SUP> at extraction intervals of 5 days. They were operated under optimal light conditions of incident light greater than <I>Chlorella v.</I> saturation constant and absorbance = 40 and at incipient churn flow (Re = 10000–11000) with dimension of fluegas bubbles around 5 mm, apt to guarantee Sh = 1500–2500; and with a calculated Da<SUB>II</SUB> around 25.</P> <P><B>Highlights</B></P> <P> <UL> <LI> Theoretical scale-up of photobioreactors by Buckingham π-theorem. </LI> <LI> Dimensionless numbers evaluated by experimental campaign at different scales. </LI> <LI> Airlift reactors for cultivation of Chlorella Vulgaris at pilot scale. </LI> <LI> Set-up and tuning of operating conditions for integration in biorefineries. </LI> </UL> </P> <P><B>Graphical abstract</B></P> <P>[DISPLAY OMISSION]</P>