Influence of design and operational parameters of a Taylor flow reactor on the bioconversion of methane to ectoines

Ectoine is one of the most attractive bioproducts due to its high market price and applications. Methanotrophic bacteria can synthesize ectoine from biogas. In this work, key design and operating parameters were optimised to maximise the bioconversion of methane to ectoine in a novel Taylor Flow bioreactor. This bioreactor configuration is characterized by higher gas-liquid mass transfer coefficients compared to conventional bubble column bioreactors. Thus, the influence of the internal gas recirculation flow rate (1.0 L·min −1 , 2.5 L·min −1 , 4.0 L·min −1 , 5.5 L·min −1 ) at 60 and 120 min of gas residence time (GRT), the liquid recirculation flow rate (0 L·h −1 , 141 L·h −1 , 165 L·h −1 , 395 L·h −1 , 434 L·h −1 ) and the capillary length (1.50 and 0.75 m) was evaluated using a mixed methanotrophic consortium. Process operation at 120 min of GRT and 5.5 L·min −1 of gas recirculation flow rate enhanced methane bioconversion, resulting in a maximum efficiency of 83.8 ± 2.7 %. The decrease in capillary length from 1.5 to 0.75 m did not enhance methane bioconversion. Intracellular ectoine and hydroxyectoine reached maximum contents of 105.1 ± 8.6 mg EC ·g TSS −1 and 33.4 ± 11.7 mg HE ·g TSS −1 , respectively. Nitratireductor was the dominant genus, while Methylomicrobium and Methylophaga were the main methanotrophic bacteria detected in the consortium. This study confirmed the feasibility of bioconverting novel renewable feedstocks such biogas into high-added value bio-products, boosting the circular and carbon neutral economy in bio-based industries. • Taylor flow improved methane gas-liquid mass transfer. • High gas and liquid recirculation flow rates promoted methane bioconversion. • Higher gas residence times improved CH4 bioconversion efficiency. • Higher carbon loading rates increased ectoine and hydroxyectoine biosynthesis. • The 2-fold decrease in capillary length entailed lower CH4 bioconversions.

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Publication Details

Journal
Journal of environmental chemical engineering
Published
2024-10-02
DOI
https://doi.org/10.1016/j.jece.2024.114323
Citations
9
Primary Topic
Fluid Dynamics and Mixing
Type
article
Field-Weighted Citation Impact
1.66

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article

Influence of design and operational parameters of a Taylor flow reactor on the bioconversion of methane to ectoines

Frank Rogalla, Raquel Lebrero, Victor M. Monsalvo, Raquel Herrero‐Lobo et al.
9 citations
Journal of environmental chemical engineering
Fluid Dynamics and Mixing
1.66
article

Influence of design and operational parameters of a Taylor flow reactor on the bioconversion of methane to ectoines

Frank Rogalla, Raquel Lebrero, Victor M. Monsalvo, Raquel Herrero‐Lobo, Andrés F. Torres-Franco, Raúl Muñoz, María del Rosario Rodero, Patricia Zamora, Wendy Mylene Llamas-Ramos
article en
9 citations

Abstract

Ectoine is one of the most attractive bioproducts due to its high market price and applications. Methanotrophic bacteria can synthesize ectoine from biogas. In this work, key design and operating parameters were optimised to maximise the bioconversion of methane to ectoine in a novel Taylor Flow bioreactor. This bioreactor configuration is characterized by higher gas-liquid mass transfer coefficients compared to conventional bubble column bioreactors. Thus, the influence of the internal gas recirculation flow rate (1.0 L·min −1 , 2.5 L·min −1 , 4.0 L·min −1 , 5.5 L·min −1 ) at 60 and 120 min of gas residence time (GRT), the liquid recirculation flow rate (0 L·h −1 , 141 L·h −1 , 165 L·h −1 , 395 L·h −1 , 434 L·h −1 ) and the capillary length (1.50 and 0.75 m) was evaluated using a mixed methanotrophic consortium. Process operation at 120 min of GRT and 5.5 L·min −1 of gas recirculation flow rate enhanced methane bioconversion, resulting in a maximum efficiency of 83.8 ± 2.7 %. The decrease in capillary length from 1.5 to 0.75 m did not enhance methane bioconversion. Intracellular ectoine and hydroxyectoine reached maximum contents of 105.1 ± 8.6 mg EC ·g TSS −1 and 33.4 ± 11.7 mg HE ·g TSS −1 , respectively. Nitratireductor was the dominant genus, while Methylomicrobium and Methylophaga were the main methanotrophic bacteria detected in the consortium. This study confirmed the feasibility of bioconverting novel renewable feedstocks such biogas into high-added value bio-products, boosting the circular and carbon neutral economy in bio-based industries. • Taylor flow improved methane gas-liquid mass transfer. • High gas and liquid recirculation flow rates promoted methane bioconversion. • Higher gas residence times improved CH4 bioconversion efficiency. • Higher carbon loading rates increased ectoine and hydroxyectoine biosynthesis. • The 2-fold decrease in capillary length entailed lower CH4 bioconversions.

Journal of environmental chemical engineeringVol. 12(6)
Universidad de Valladolid (ES), Centro de Estudios y Experimentación de Obras Públicas (ES)
European Commission, Junta de Castilla y León, HORIZON EUROPE Framework Programme, European Regional Development Fund, FP7 Coordination of Research Activities
Affordable and clean energy
Openalex Percentile: Top 17%
Fluid Dynamics and Mixing
1.66
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