Biomethanation of Syngas by Enriched Mixed Anaerobic Consortia in Trickle Bed Reactors

Two identical trickle-bed reactor setups were designed and operated under mesophilic conditions and atmospheric pressure, without pH control, for the biomethanation of syngas consisted of 45% H2, 25% CO2, 20% CO and 10% CH4. The reactors were inoculated with mixed methanogenic microbial consortia formerly adapted to the gaseous mixture.

During the start-up of the reactors acetic acid accumulation in the liquid broth resulted in a pH decrease to levels unfavorable for methanogenic activity. This was corrected by introducing a strong phosphate buffer in the medium (K2HPO4/KH2PO4 : 87 mM/13 mM). Channeling phenomena observed across the trickle bed were eliminated by setting a high liquid recirculation rate (1600 l/lbed/d).

The reactors were operated for 294 days presenting minor deviations between them at the 24 extracted steady states and high cell retention even at a hydraulic retention time (HRT) of 3.7 days. At a gas residence time of 2.31 h and a HRT of 5.5 days the achieved CH4 productivity was 2 mmol/lbed/h with 93% H2 and 90% CO conversion efficiency and a 78% electron yield to CH4.

The conducted study verified that an enriched methanogenic microbial consortium can effectively convert syngas to CH4 in a trickle bed reactor under appropriate operational conditions.