Abstract The limited gas–liquid mass transfer represents the main challenge in the operation of cost-effective bioreactors devoted to the treatment of poorly soluble gas pollutants such as methane (CH 4… Click to show full abstract
Abstract The limited gas–liquid mass transfer represents the main challenge in the operation of cost-effective bioreactors devoted to the treatment of poorly soluble gas pollutants such as methane (CH 4 ). This study evaluates the influence of internal gas-recycling strategies on the enhancement of CH 4 abatement in a bubble column bioreactor inoculated with the methanotroph Methylocystis hirsuta . Maximum CH 4 removal efficiencies of 72.9 ± 0.5% (corresponding to elimination capacities of 35.2 ± 0.4 g m −3 h −1 ) were recorded under process operation at an empty bed residence time of 30 min and 0.50 m 3 gas m −3 reactor min −1 of internal gas-recycling rate. The accumulation of poly-3-hydroxybutyrate (PHB) in M. hirsuta was evaluated batchwise under limitations of potassium, manganese, nitrogen, and nitrogen with excess of iron. Nitrogen starvation resulted in the highest PHB content (28 ± 1%). Likewise, the implementation of sequential N starvation cycles in a continuous bubble column reactor operated at a gas residence time of 30 min and an internal gas-recycling rate of 0.50 m 3 gas m −3 reactor min −1 supported a PHB content of up to 34.6 ± 2.5%, with a volumetric PHB productivity of 1.4 ± 0.4 kg m −3 d −1 and elimination capacities of 16.2 ± 9.5 g m −3 h −1 .
               
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