Evaluation of microporous hollow fibre membranes for mass transfer of H₂ into anaerobic digesters for biomethanisation

Abstract

BACKGROUND With high surface‐to‐volume ratios, hollow fibre membranes offer a potential solution to improving gas–liquid mass transfer. This work experimentally determined the mass transfer characteristics of commercially available microporous hollow fibre membranes and compared these with the mass transfer from bubble column reactors. Both mass transfer systems are considered for biological methanization, a process that faces a challenge to enhance the H₂ gas–liquid mass transfer for methanogenic Archaea to combine H₂ and CO₂ into CH₄.
RESULTS Polypropylene membranes showed the highest mass transfer rate of membranes tested, with a mass transfer coefficient for H₂ measured as k_L = 1.2 × 10⁻⁴ ms⁻¹. These results support the two‐film gas–liquid mass transfer theory, with higher mass transfer rates measured with an increase in liquid flow velocity across the membrane. Despite the higher mass transfer rate from polypropylene membranes and with a liquid flow across the membrane, a volumetric surface area of α = 10.34 m⁻¹ would be required in a full‐scale in situ biological methanization process with much larger values potentially required for high‐rate ex situ systems.
CONCLUSIONS The large surface area of hollow fibre membranes required for H₂ mass transfer and issues of fouling and replacement costs of membranes are challenges for hollow fibre membranes in large‐scale biological methanization reactors. Provided that the initial bubble size is small enough (d_e < 0.5 mm), calculations indicate that microbubbles could offer a simpler means of transferring the required H₂ into the liquid phase at a head typical of that found in commercial‐scale anaerobic digesters.

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Identifiers

ORCID for Sonia Heaven: orcid.org/0000-0001-7798-4683

ORCID for Charles Banks: orcid.org/0000-0001-6795-814X

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