Carone, Michele, Alpe, Davis, Costantino, Valentina, Derossi, Clara, Occhipinti, Andrea, Zanetti, Mariachiara, and Riggio, Vincenzo A.
Microalgae-based biorefinery processes are gaining particular importance as a biotechnological tool for direct carbon dioxide fixation and production of high-quality biomass and energy feedstock for different industrial markets. However, despite the many technological advances in photobioreactor designs and operations, microalgae cultivation is still limited due to the low yields achieved in open systems and to the high investment and operation costs of closed photobioreactors. In this work, a new alveolar flat panel photobioreactor was designed and characterized with the aim of achieving high microalgae productivities and CO 2 bio-fixation rates. Moreover, the energy efficiency of the employed pump-assisted hydraulic circuit was evaluated. The 1.3 cm thick alveolar flat-panels enhance the light utilization, whereas the hydraulic design of the photobioreactor aims to improve the global CO 2 gas-liquid mass transfer coefficient (k L aCO 2). The mixing time, liquid flow velocity, and k L aCO 2 as well as the uniformity matrix of the artificial lighting source were experimentally calculated. The performance of the system was tested by cultivating the green microalga Acutodesmus obliquus. A volumetric biomass concentration equal to 1.9 g L−1 was achieved after 7 days under controlled indoor cultivation conditions with a CO 2 bio-fixation efficiency of 64% of total injected CO 2. The (gross) energy consumption related to substrate handling was estimated to be between 27 and 46 Wh m−3, without any cost associated to CO 2 injection and O 2 degassing. The data suggest that this pilot-scale cultivation system may constitute a relevant technology in the development of microalgae-based industrial scenario for CO 2 mitigation and biomass production. [Display omitted] • New alveolar flat panel photobioreactor with positive pressure-serpentine circulation. • CO 2 supply strategy enhancing the global CO 2 mass transfer coefficient (k L aCO 2). • Low energy demand for liquid culture circulation and mixing. • Acutodesmus obliquus mean daily volumetric productivity of 0.21 g L−1 d−1. • CO 2 bio-fixation efficiency equal to 64% of total injected CO 2. [ABSTRACT FROM AUTHOR]