Assessing the temperature effect on the kinetics of a hydrogenotrophic methanogenic culture using a novel headspace-free methodology
• Headspace-free methodology enables continuous monitoring of dissolved H₂ kinetics. • H₂ uptake rate increases with temperature, reaching 773 mmol H₂·gVSS⁻¹·d⁻¹ at 65°C. • PHF-HUR avoids gas-liquid transfer limitations. Time is reduced compared to SBT. • Temperature dependent half-saturation constant ranges from 4.27·10⁻³ to 6.87·10⁻² mM. • Moser model fits microbial kinetics better than Monod across tested conditions. Accurately determining the biological activity of hydrogenotrophic microbial cultures independently of potential gas-liquid mass transfer limitations for hydrogen is important but is challenging. In this work, a novel methodology called Pressurized Headspace-Free Hydrogen Uptake Rate (PHF-HUR) is presented and validated. The methodology consists on first saturating a microbial culture bubbling pure H 2 under selected pressures in a 120 mL stirred batch bioreactor equipped with a dissolved H 2 probe. Secondly, the decrease of the dissolved H 2 concentration under headspace-free conditions is monitored in real-time. Hydrogen profiles under headspace-free conditions are used to calculate the HUR and to assess the microbial activity and related kinetics. A mixed culture was characterized at different temperatures ranging from 27 °C to 70 °C using this methodology. Modelling of hydrogen uptake rate was conducted using Monod and Moser kinetic equations, the latter providing a better fit of the experimental data. In the novel PHF-HUR methodology, hydrogen uptake increased with temperature reaching 773 mmol H2 ·g VSS −1 ·d −1 at 65 °C, but was nil at 70 °C. The half-saturation concentration for the methanogens was also temperature dependent, ranging from 4.3·10 −3 mM H 2 at 27 °C to 6.9·10 −2 mM at 65 °C. Results indicate the potential of the novel methodology to accurately determine the biological kinetics of hydrogenotrophic methanogens without gas-liquid mass transfer limitations.
Authors
- Daniel González (ORCID: https://orcid.org/0000-0003-0128-6445)
- David Gabriel (ORCID: https://orcid.org/0000-0002-7713-4192)
- Marc A. Deshusses (ORCID: https://orcid.org/0000-0003-0639-7865)
- Pablo Hernández Benavides (ORCID: https://orcid.org/0009-0003-0592-6558)
- Javier Lafuente (ORCID: https://orcid.org/0000-0002-4601-9001)
- Àlex Gaona (ORCID: https://orcid.org/0000-0002-6912-5333)
- Manuel Fachal-Suárez (ORCID: https://orcid.org/0000-0002-4244-6831)
Institutions
- Universitat Autònoma de Barcelona (ES)
- Duke University (US)
Publication Details
- Journal
- Chemical Engineering Journal Advances
- Published
- 2025-11-01
- DOI
- https://doi.org/10.1016/j.ceja.2025.100951
- Primary Topic
- Anaerobic Digestion and Biogas Production
- Type
- article
- Field-Weighted Citation Impact
- 0.00