Methane biodegradation in a two-phase partition internal loop airlift reactor with gas recirculation

✍ Scribed by José Rocha-Rios; Guillermo Quijano; Frédéric Thalasso; Sergio Revah; Raul Muñoz

• Publisher: Wiley (John Wiley & Sons)
• Year: 2010
• Tongue: English
• Weight: 232 KB
• Volume: 86
• Category: Article
• ISSN: 0268-2575
• DOI: 10.1002/jctb.2523

✦ Synopsis

Abstract

BACKGROUND: The potential of organic liquid solvents and solid polymers to enhance CH~4~ mass transfer was studied in a two‐phase partition internal loop airlift reactor operated with gas recirculation under biotic and abiotic conditions. A preliminary screening of the most common liquid solvents (silicone oil 20 cSt, silicone oil 200 cSt and 2,2,4,4,6,8,8‐heptametilnonane) and solid polymers (Kraton® G6157, Desmopan® DP9370A and Elvax® 880) resulted in the selection of silicone oil 200 cSt (S200) and Desmopan DP9370A (D9370) for further investigation based on their high affinity for CH~4~, biocompatibility and nonbiodegradability.

RESULTS: Under abiotic conditions, the increase in gas recirculation from 0 to 1 vvm in the absence of a transfer vector increased the overall mass transfer coefficient for oxygen (k~L~a) by 195%. The presence of S200 and D9370 at 10% (v/v) under operation at 1 vvm of gas recirculation rate mediated an increase in k~L~a of 100% and 136%, respectively. Likewise, the increase in gas recirculation from 0 to 1 vvm in the absence of a transfer vector and in the presence of S200 during the continuous biodegradation of methane at 3% (v/v) and 7.3 min empty bed residence time resulted in increases in CH~4~ removal and CO~2~ production rates of 47% and 36%, respectively. Nevertheless, no significant enhancement in CH~4~ removal due to the presence of 10% of Desmopan or silicone oil was recorded under operation at 1 vvm.

CONCLUSIONS: These results suggest that microbial activity rather than mass transport could be the limiting step in biological CH~4~ abatement in this system, contrary to that observed in previous studies with stirred tank reactors, where the organic phase addition increased methane biodegradation. Copyright © 2010 Society of Chemical Industry