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Fig. 3 | Biotechnology for Biofuels and Bioproducts

Fig. 3

From: Carbon and energy balance of biotechnological glycolate production from microalgae in a pre-industrial scale flat panel photobioreactor

Fig. 3

Growth and glycolate production of Chlamydomonas reinhardtii in a flat panel reactor. Biomass (A), cell numbers (B), Chl a concentration (C), QPhar (D), Fv/Fm (E), and glycolate accumulation (F) of two independent runs (run 1: open symbols; run 2: closed symbols). During the biomass phase (green shading), cultures were grown with 2% CO2 in ambient air. Glycolate production was induced by switching aeration to 0.2% CO2, 35% O2 in ambient air. Arrows mark the time of additional 7 mM NH4+ supply. The horizontal dashed line in (D) indicates the irradiated photosynthetically available radiation (PAR) of 250 µ mol photons m−2 s−1

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