Hydrodynamic and mass transfer characterization of a flat-panel airlift photobioreactor with high light path

Abstract This work evaluates the volumetric mass transfer coefficient ( k L a ), the gas hold-up ( ɛ ) and the mixing time ( t m ) as a function of superficial gas velocity ( U G ) in a flat-panel photobioreactor (PBR) with high light path. CO 2 utilization efficiency and volumetric power consumption ( P / V ) were also evaluated. A 50 L working volume photobioreactor was developed, 0.67 m in length, 0.57 m in height and 0.15 m in width (light path). The height-width ratio was 3.8, which is lower than reported in most PBRs. Initially, experiments were performed with air and tap water (biphasic system) and, subsequently, using a Spirulina sp. culture (triphasic system: air, culture medium, cells). Minimum and maximum superficial gas velocity values were 5 × 10 −5 and 8.4 × 10 −3  m s −1 , respectively. Maximum values for k L a and ɛ were 20.34 h −1 (0.0057 s −1 ) and 0.033 in the biphasic system, and 31.27 h −1 (0.0087 s −1 ) and 0.065 in the triphasic system. CO 2 utilization efficiency was 30.57%. Results indicate that the hydrodynamic and mass transfer characteristics of this photobioreactor are more efficient than those reported elsewhere for tubular and other flat-plate PBRs, which opens the possibility of using PBRs with higher light paths than yet proposed.